Process and plant for producing sulfuric acid
View Patent ↗There are described a process and a plant for producing sulfuric acid by catalytic oxidation of SO 2 to SO 3 and subsequent absorption of SO 3 in sulfuric acid, wherein the SO 3 is introduced into a first absorption stage and absorbed there in concentrated sulfuric acid, wherein the sulfuric acid having a higher concentration due to the absorption is passed through a heat exchanger and cooled, and wherein the non-absorbed SO 3 is supplied to a second absorption stage for the further absorption in sulfuric acid. Before the first absorption stage a partial stream of SO 3 is branched off and supplied directly to the second absorption stage.
1. A process for producing sulfuric acid by catalytic oxidation of SO 2 to SO 3 and subsequent absorption of SO 3 in sulfuric acid, comprising
introducing the SO 3 into a first absorption stage comprising a primary absorber and absorbing the SO 3 in concentrated sulfuric acid;
passing the sulfuric acid having a higher concentration due to the absorption through a heat exchanger and cooling and;
supplying the non absorbed SO 3 to a second absorption stage comprising a secondary absorber for further absorption into sulfuric acid,
wherein before the primary absorber, a partial stream of SO 3 is branched off and supplied directly to another absorber.
2. The process as claimed in claim 1 , wherein at least part of the sulfuric acid stream cooled in the heat exchanger is recirculated to the first absorption stage.
3. The process as claimed in claim 2 , wherein the sulfuric acid stream recirculated to the first absorption stage is diluted with process water.
4. The process as claimed in claim 1 , wherein air or SO 2 gas is dried in a drying tower by means of sulfuric acid, wherein the drying tower is operated with the same sulfuric acid concentration as the absorbers.
5. The process as claimed in claim 4 , wherein the absorbers and the drying tower are supplied with sulfuric acid by a common storage tank.
6. A plant for producing sulfuric acid by catalytic oxidation of
SO 2 to SO 3 and subsequent absorption of SO 3 in sulfuric acid, comprising
a SO 3 supply conduit,
a primary absorber, to which gaseous SO 3 and concentrated sulfuric acid are supplied, and
a secondary absorber, to which the SO 3 not absorbed in the primary absorber is supplied for the further absorption in sulfuric acid,
wherein a bypass conduit which is branched off from the SO 3 supply conduit before the primary absorber is coupled to the secondary absorber, in order to directly supply thereto a partial stream of SO 3 .
7. The plant as claimed in claim 6 , wherein the bypass conduit includes a valve for adjusting the partial stream of SO 3 passed by the primary absorber.
8. The plant as claimed in claim 6 , wherein the absorbers and a drying tower for drying air by means of sulfuric acid are coupled to a common storage tank for supplying sulfuric acid.