US3941810A — Sulfonation of aromatic compounds in the presence…

Claim 1

Independent Claim 205 words

A process for the sulfonation of aromatic compounds selected from the group consisting of benzene, thiophene, bromobenzene, toluene, ortho-xylene, meta-xylene, anisole, naphthalene, nitro-naphthalene, anthracene and tetrahydro-naphthalene, wherein: 1. said aromatic compound is admixed with an organic solvent substantially inert to the action of sulfur trioxide under the sulfonation conditions to form a liquid mixture, and said organic solvent is admixed in a quantity of from 20% to 200% by weight based on the weight of aromatic compound, and said organic solvent is selected from the group consisting of n-pentane, n-hexane, n-heptane, iso-heptane, cyclohexane, methylcyclohexane, diethyl ether, dioxane, nitromethane and 1,1,2,2-tetrachloroethane; 2. The liquid mixture is brought to boiling in a reaction chamber at a temperature of from 20°C to 100°C at a pressure of 0.1 mm Hg to atmospheric pressure; 3. gaseous sulfur trioxide is introduced into the boiling liquid mixture within the reaction chamber to react exothermically with the aromatic compopund, said aromatic compound being employed in an excess quantity to maintain the constant presence of some unreacted aromatic compound in the reaction chamber during the sulfonation reaction, heat liberated in the exothermic sulfonation reaction causing the mixture to continue to boil and furnishing the latent heat of volatilization of the matter that volatilizes;

Claim 2

Dependent Claim 205 words

A process for the sulfonation of aromatic compounds selected from the group consisting of benzene, thiophene, bromobenzene, toluene, ortho-xylene, meta-xylene, anisole, naphthalene, nitro-naphthalene, anthracene and tetrahydro-naphthalene, wherein: 1. said aromatic compound is admixed with an organic solvent substantially inert to the action of sulfur trioxide under the sulfonation conditions to form a liquid mixture, and said organic solvent is admixed in a quantity of from 20% to 200% by weight based on the weight of aromatic compound, and said organic solvent is selected from the group consisting of n-pentane, n-hexane, n-heptane, iso-heptane, cyclohexane, methylcyclohexane, diethyl ether, dioxane, nitromethane and 1,1,2,2-tetrachloroethane; 2. The liquid mixture is brought to boiling in a reaction chamber at a temperature of from 20°C to 100°C at a pressure of 0.1 mm Hg to atmospheric pressure; 3. gaseous sulfur trioxide is introduced into the boiling liquid mixture within the reaction chamber to react exothermically with the aromatic compopund, said aromatic compound being employed in an excess quantity to maintain the constant presence of some unreacted aromatic compound in the reaction chamber during the sulfonation reaction, heat liberated in the exothermic sulfonation reaction causing the mixture to continue to boil and furnishing the latent heat of volatilization of the matter that volatilizes;

Claim 3

Dependent Claim 167 words

the matter thus volatilized is reconverted to liquid in a heat-exchanger, so that the latent heat of volatilization is exchanged in the heat-exchanger and heat liberated in the sulfonation reaction is thus removed from the reaction chamber; 5. the volatilized matter reconverted to liquid in the heat-exchanger is recycled to the reaction chamber; and 6. the pressure in the reaction chamber and the rate at which the gaseous sulfur trioxide is introduced into the liquid mixture within the reaction chamber are so controlled that matter is volatilized, reconverted to the liquid state and recycled to the reaction chamber at such a rate as to ensure that there is always present in the mixture within the reaction chamber an amount of volatilizable matter exceeding that amount capable of being volatilized by the heat of reaction of the aromatic compound present with the gaseous sulfur trioxide in contact with said aromatic compound in the reaction chamber and that the temperature of the reaction mixture is from 20°C to 100°C.

Claim 4

Dependent Claim 167 words

the matter thus volatilized is reconverted to liquid in a heat-exchanger, so that the latent heat of volatilization is exchanged in the heat-exchanger and heat liberated in the sulfonation reaction is thus removed from the reaction chamber; 5. the volatilized matter reconverted to liquid in the heat-exchanger is recycled to the reaction chamber; and 6. the pressure in the reaction chamber and the rate at which the gaseous sulfur trioxide is introduced into the liquid mixture within the reaction chamber are so controlled that matter is volatilized, reconverted to the liquid state and recycled to the reaction chamber at such a rate as to ensure that there is always present in the mixture within the reaction chamber an amount of volatilizable matter exceeding that amount capable of being volatilized by the heat of reaction of the aromatic compound present with the gaseous sulfur trioxide in contact with said aromatic compound in the reaction chamber and that the temperature of the reaction mixture is from 20°C to 100°C.

Claim 5

Dependent Claim 35 words

A process according to claim 1, in which the pressure in the reaction chamber when the sulfur trioxide is introduced into the liquid mixture within the reaction chamber is from 25 to 400 mm Hg.

Claim 6

Dependent Claim 26 words

A process according to claim 1, in which the gaseous sulfur trioxide is introduced in substantially pure form into the liquid mixture within the reaction chamber.

Claim 7

Dependent Claim 85 words

A process according to claim 1, wherein the process is operated continuously, the aromatic compound and substantially inert organic solvent being continuously fed into the reaction chamber to form a liquid mixture, the sulfur trioxide being continuously introduced into the liquid mixture while this is boiling therein, the resultant reaction mixture being continuously withdrawn from the reaction chamber, and both the substantially inert organic solvent and the unreacted aromatic compound being separated from the sulfonated aromatic compound and purified and recycled to the reaction chamber.

Annuity Stage	Window Opens	Payment Deadline	Surcharge Period Until	Estimated Fee	Status
3.5 Years (Year 4)	1979-03-02	1979-09-01	1980-03-02	$2000.00	Window Closed / Lapsed
7.5 Years (Year 8)	1983-03-02	1983-09-01	1984-03-02	$3760.00	Window Closed / Lapsed
11.5 Years (Year 12)	1987-03-02	1987-09-01	1988-03-02	$7700.00	Window Closed / Lapsed

Sulfonation of aromatic compounds in the presence of solvents

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