Process for regenerating sulfuric acid

Claim 2

A process for regenerating contaminated 70 to 90% by weight sulfuric acid containing water, which comprises distilling said contaminated sulfuric acid at a pressure of 5 to 12 torrs, condensing the distilling vapors containing sulfuric acid and water, withdrawing non-volatile distillation bottoms products; and concentrating the distillation condensate in a Pauling apparatus comprising a dephlegmator and a vessel, said vessel containing 96 to 97% by weight sulfuric acid, by heating said vessel to maintain the sulfuric acid at a boiling temperature, feeding said distillation condensate to the dephlegmator, stripping water from the condensate and concentrating the sulfuric acid in the vessel up to 96 to 97% by weight.

Claim 3

The process of claim 1 in which the contaminated sulfuric acid contains aromatic mono-and/or polycarboxylic acids and light and/or heavy metal salts thereof as impurities.

Claim 4

The process of claim 1 which comprises carrying out the distillation at a temperature of up to 200° C.

Claim 5

The process of claim 1 in which the distillation is carried out at a pressure of from 8 to 12 torrs.

Claim 6

The process of claim 1 in which the contaminated sulfuric acid is contacted with an inert absorbent prior to distillation.

Claim 7

The process of claim 5 in which 1 to 5% by weight of absorbents are added to the contaminated acid.

Claim 8

The process of claim 1 in which the contaminated sulfuric acid contains up to 2% by weight of organic impurities, based on carbon content.

Claim 9

The process of claim 1 in which the contaminated sulfuric acid contains aromatic mono and/or polycarboxylic acid impurities.

Claim 10

The process of claim 1 in which the contaminated sulfuric acid contains organic nitrogen compound impurities.

Claim 11

The process of claim 1 in which the contaminated sulfuric acid contains light and/or heavy metal salt impurities.

Claim 12

The process of claim 10 which comprises, during the distillation and condensing of the sulfuric acid, precipitating in the distillation apparatus and separating from the distillation bottoms heavy metal sulfate precipitates.

Claim 13

The process of claim 1 in which the contaminated sulfuric acid contains ammonium ions or forms ammonium ions during the distillation step.

Claim 14

The process of claim 1 which comprises adding to the contaminated sulfuric acid inorganic, positive 3 and/or 5 valent nitrogen compounds.

Claim 15

The process of claim 1 which comprises adding to the contaminated sulfuric acid 0.1 to 5% by weight of nitric acid or hydrogen peroxide.

Claim 16

The process of claim 1 which comprises continuously introducing the contaminated sulfuric acid into a volume of boiling sulfuric acid in the distillation apparatus, continuously distilling and condensing water and sulfuric acid, and continuously feeding the distillation condensate to the dephlegmator portion of the Pauling apparatus and continuously withdrawing 96 to 97% concentrated sulfuric acid from the vessel portion of the Pauling apparatus.

Claim 17

The process of claim 1 in which the contaminated sulfuric acid contains aromatic mono-and/or polycarboxylic acids, organic nitrogen compounds and light and/or heavy metal and ammonium salts thereof as impurities.

Claim 18

A process for regenerating contaminated aqueous 70 to 90% by weight sulfuric acid containing up to 2% by weight organic impurities, based on carbon content, selected from the group consisting of aromatic mono- and polycarboxylic acids, organic nitrogen compounds and salts of light and/or heavy metal ions and ammonium ions, which comprises adding about 1 to 5% by weight nitric acid to the contaminated sulfuric acid, distilling the contaminated acid in a distillation apparatus, at a pressure of 5 to 12 torrs and at a temperature of up to 200° C, condensing the distillation vapors which contain water and sulfuric acid, withdrawing nonvolatile distillation bottoms products, feeding the distillation condensate to the dephlegmator portion of a Pauling apparatus, which apparatus comprises a vessel portion containing 96 to 97% by weight boiling sulfuric acid, stripping water from the condensate and concentrating the condensate sulfuric acid in the vessel portion up to 96 to 97% sulfuric acid.

Claim 19

A process for regenerating contaminated aqueous 70 to 90% by weight sulfuric acid containing up to 2% by weight organic impurities, based on carbon content, selected from the group consisting of aromatic mono- and polycarboxylic acids, organic nitrogen compounds and salts of light and/or heavy metal ions and ammonium ions, which comprises adding about 1 to 5% by weight nitric acid to the contaminated sulfuric acid, distilling the contaminated acid in a distillation apparatus, at a pressure of 5 to 12 torrs and at a temperature of up to 200° C, condensing the distillation vapors which contain water and sulfuric acid, withdrawing nonvolatile distillation bottoms products, feeding the distillation condensate to the dephlegmator portion of a Pauling apparatus, which apparatus comprises a vessel portion containing 96 to 97% by weight boiling sulfuric acid, stripping water from the condensate and concentrating the condensate sulfuric acid in the vessel portion up to 96 to 97% sulfuric acid.

Claim 20

The process of claim 17 in which the contaminated sulfuric acid contains impurities selected from the group consisting of copper, iron, ammonium, alkaline earth metal and alkali metal sulfates.

Claim 21

The process of claim 17 in which 0.1 to 5% by weight nitric acid is added to the contaminated sulfuric acid.

Claim 22

The process of claim 17 in which the organic impurities comprise phthalic acid.

Claim 23

The process of claim 17 in which organic impurities are decomposed to elemental carbon during the distillation step.