Dilute sulfuric acid vacuum concentration system
A vacuum concentration and vacuum system technology, applied in the direction of sulfur trioxide/sulfuric acid, sulfur compounds, inorganic chemistry, etc., can solve problems such as high safety requirements, increased process costs, and incomplete removal of organic matter, so as to avoid blockage, Effect of increasing circulation absorption efficiency
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0043] In this embodiment, a dilute sulfuric acid vacuum concentration system is provided, including a concentration tank, a washing tower and a spray tower connected to the gas phase outlet of the concentration tank in sequence; the washing tower is provided with a first circulation pipeline to realize the dilute sulfuric acid in the liquid phase Circulation spraying in the washing tower; the spraying tower is provided with a second circulation pipeline to realize condensation of the gas phase passing into the spraying tower from the washing tower; the second circulation pipeline is connected with the first circulation pipeline, As the supplementary water of the first circulation line, to keep the content of dilute sulfuric acid in the circulation liquid constant.
[0044] In this embodiment, the vacuum concentration system provided by the present invention adopts a double-tower structure in which the washing tower and the spray tower are separated. There is no solid phase at...
Embodiment 2
[0067] This embodiment is a further improvement made on the basis of Embodiment 1, and its difference from Embodiment 1 is:
[0068] In this embodiment, a regulating valve is provided at the connection between the second circulation pipeline and the first circulation pipeline. The water in the circulation pipeline is sent into the first circulation pipeline, or the connection between the second circulation pipeline and the first circulation pipeline is closed, so that the condensed water in the waste water tank is only used as the spray liquid of the spray tower. The second circulation pipeline is unidirectionally connected to the first circulation pipeline through the regulating valve.
[0069] Other implementation modes of this embodiment are the same as embodiment 1.
Embodiment 3
[0071] Such as figure 2 As shown, this embodiment is a further improvement made on the basis of embodiment 1, and its difference with embodiment 1 is:
[0072] The bottom of the washing tower is also provided with a gas phase equilibrium pipeline connected to the feed port of dilute sulfuric acid, the raw material of the concentration tank. When the concentration of the liquid phase dilute sulfuric acid in the washing tower rises, part of the liquid phase sulfuric acid is discharged from the washing tower system to maintain the washing process. The concentration of dilute sulfuric acid in the tower and the operating temperature of the scrubber. The discharged liquid-phase sulfuric acid is returned to the raw material dilute sulfuric acid feed port of the concentration tank to increase the output of finished acid.
[0073] Other implementation modes of this embodiment are the same as embodiment 1.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 

