Reactor effluent quench system

Claim 2

In an oxychlorination reaction, a process for recovering hydrogen chloride, comprising: withdrawing a gas containing hydrogen chloride and water vapor from an oxychlorination reaction zone; contacting said gas in a first quench zone with an aqueous hydrogen chloride quench liquid to cool said gas, said contacting partially vaporizing said quench liquid to produce a remaining aqueous hydrogen chloride liquid having a hydrogen chloride concentration greater than the hydrogen chloride concentration of said quench liquid; introducing said remaining aqueous hydrogen chloride liquid into said oxychlorination reaction zone; further cooling cooled gas from said first quench zone in a second quench zone to produce aqueous hydrogen chloride having a hydrogen chloride concentration from about 8 to about 20 percent, by weight; and passing aqueous hydrogen chloride from said second quench zone to said first quench zone as said aqueous hydrogen chloride quench liquid.

Claim 3

The process of claim 1 wherein said second quench zone is a direct contact quench zone and said further cooling is effected by direct contact with aqueous hydrogen chloride.

Claim 4

The process of claim 2 wherein the gas is cooled in said direct contact quench zone to a temperature from about 220°F. to about 250°F.

Claim 5

The process of claim 3 wherein said cooled gas is further cooled to a temperature from about 140°F. to about 160°F.

Claim 6

In the oxidation of a molten salt, a process for recovering hydrogen chloride, comprising: contacting in a reaction zone a molten salt mixture comprising a multivalent metal chloride in its higher and lower valence states with gaseous molecular oxygen, gaseous hydrogen chloride and an aqueous solution of hydrogen chloride to produce the oxychloride of the multivalent metal and to recover hydrogen chloride by enriching the higher valent metal chloride content of the molten mixture; withdrawing a gas containing hydrogen chloride and water vapor from the reaction zone; contacting said gas in a first quench zone with an aqueous hydrogen chloride quench liquid to cool said gas, said contacting partially vaporizing said quench liquid to produce a remaining aqueous hydrogen chloride liquid having a hydrogen chloride concentration greater than the hydrogen chloride concentration of said quench liquid; introducing said remaining aqueous hydrogen chloride liquid into said reaction zone as said aqueous hydrogen chloride; further cooling cooled gas from said first quench zone in a second quench zone to produce aqueous hydrogen chloride having a hydrogen chloride concentration from about 8 to about 20 percent, by weight; and passing aqueous hydrogen chloride from said second quench zone to said first quench zone as said aqueous hydrogen chloride quench liquid.

Claim 7

In the oxidation of a molten salt, a process for recovering hydrogen chloride, comprising: contacting in a reaction zone a molten salt mixture comprising a multivalent metal chloride in its higher and lower valence states with gaseous molecular oxygen, gaseous hydrogen chloride and an aqueous solution of hydrogen chloride to produce the oxychloride of the multivalent metal and to recover hydrogen chloride by enriching the higher valent metal chloride content of the molten mixture; withdrawing a gas containing hydrogen chloride and water vapor from the reaction zone; contacting said gas in a first quench zone with an aqueous hydrogen chloride quench liquid to cool said gas, said contacting partially vaporizing said quench liquid to produce a remaining aqueous hydrogen chloride liquid having a hydrogen chloride concentration greater than the hydrogen chloride concentration of said quench liquid; introducing said remaining aqueous hydrogen chloride liquid into said reaction zone as said aqueous hydrogen chloride; further cooling cooled gas from said first quench zone in a second quench zone to produce aqueous hydrogen chloride having a hydrogen chloride concentration from about 8 to about 20 percent, by weight; and passing aqueous hydrogen chloride from said second quench zone to said first quench zone as said aqueous hydrogen chloride quench liquid.

Claim 8

The process of claim 5 wherein the gas is cooled in said second quench zone to a temperature from about 220°F. to about 250°F.

Claim 9

The process of claim 6 wherein said cooled gas is further cooled to a temperature from about 140°F. to about 160°F.

Claim 10

The process of claim 7 wherein said multivalent metal chloride is copper chloride.

Claim 11

The process of claim 1 wherein a portion of the aqueous hydrogen chloride from the second quench zone is employed to directly cool the gas containing hydrogen chloride and water vapor prior to the first quench zone, resulting in complete vaporization of said portion of the aqueous hydrogen chloride from the second quench zone.

Claim 12

The process of claim 5 wherein a portion of the aqueous hydrogen chloride from the second quench zone is employed to directly cool the gas containing hydrogen chloride and water vapor prior to the first quench zone, resulting in complete vaporization of said portion of the aqueous hydrogen chloride from the second quench zone.

Claim 13

The process of claim 1 wherein said aqueous hydrogen chloride has a hydrogen chloride concentration from about 8 to about 16 percent, by weight.

Claim 14

The process of claim 5 wherein said aqueous hydrogen chloride has a hydrogen chloride concentration from about 8 to about 16 percent, by weight.