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On-line purification method of hydrochloric acid in the production of potassium sulfate by Mannheim process

A Mannheim method, potassium sulfate technology, applied in the direction of sulfate/bisulfate preparation, chemical instruments and methods, inorganic chemistry, etc., can solve the problems of high impurity content of hydrochloric acid, economic loss of enterprises, low quality, etc., and achieve hydrochloric acid Good quality, no energy consumption, low cost effect

Active Publication Date: 2022-07-22
CHINA THREE GORGES UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, because the Mannheim method produces a small amount of impurities such as water vapor, sulfuric acid gas, potassium sulfate dust, and potassium chloride dust in the hydrogen chloride gas, these impurities and hydrogen chloride gas exist in the form of mist, according to current mature technical methods (such as figure 1 ) after absorption, the hydrochloric acid obtained has high impurity content, low quality, and limited use. The enterprise even needs to pay additional expenses to entrust others to consume and use it, which brings certain economic losses to the enterprise.

Method used

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  • On-line purification method of hydrochloric acid in the production of potassium sulfate by Mannheim process
  • On-line purification method of hydrochloric acid in the production of potassium sulfate by Mannheim process
  • On-line purification method of hydrochloric acid in the production of potassium sulfate by Mannheim process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] The hydrochloric acid B in the first-stage washing tower was pumped into the hydrochloric acid distillation column (flow rate was 14.16L / min), and introduced into the hydrochloric acid distillation tower at 245°C and the flow rate was 10m. 3 / s of combustion chamber exhaust for distillation. The flow rate of the residual liquid entering the primary washing tower is 7.08L / min, and the leaching liquid is condensed into the acid storage tank to obtain food-grade hydrochloric acid. Food-grade hydrochloric acid has clear color, sulfate content of 0.002%, iron salt content of 0.0005%, acid concentration of 32.7%, and an output of 15 tons / day.

[0041] Deionized water (flow rate of 9.44L / min) washes the hydrogen chloride gas in the four-stage washing tower, enters the three-stage falling film absorption tower to absorb the hydrogen chloride gas, and the hydrogen chloride tail gas generated in the distillation tower also directly enters the three-stage falling film absorption to...

Embodiment 2

[0044] The hydrochloric acid B in the first-stage washing tower was drawn into the hydrochloric acid distillation column (flow rate was 14.16L / min), and was introduced into the hydrochloric acid distillation tower at 295°C and the flow rate was 14m. 3 / s of combustion chamber exhaust for distillation. The flow rate of the residual liquid entering the first-level washing tower is 3.54L / min, and the leaching liquid is condensed into the acid storage tank to obtain food-grade hydrochloric acid. Food grade hydrochloric acid is clear in color, sulfate content is 0.001%, iron salt content has no clear value, acid concentration is 33.6%, and the output is 10 tons / day.

[0045] Deionized water (flow rate of 11.80L / min) washes the hydrogen chloride gas in the four-stage washing tower, and enters the three-stage falling film absorption tower to absorb the hydrogen chloride gas, and the hydrogen chloride tail gas generated in the distillation tower also directly enters the three-stage fa...

Embodiment 3

[0048] The hydrochloric acid B in the first-stage washing tower was drawn into the hydrochloric acid distillation column (flow rate was 9.44L / min), and was introduced into the hydrochloric acid distillation tower at 260°C and the flow rate was 13.7m. 3 / s of combustion chamber exhaust for distillation. The flow rate of the residual liquid entering the first-stage washing tower is 3.14L / min, and the leachate is condensed into the acid storage tank to obtain food-grade hydrochloric acid. Food-grade hydrochloric acid has clear color, sulfate content of 0.001%, iron salt content of 0.0005%, acid concentration of 32.1%, and an output of 13.3 tons / day.

[0049] Deionized water (flow rate of 10.24L / min) washes the hydrogen chloride gas in the four-stage washing tower, and enters the three-stage falling film absorption tower to absorb the hydrogen chloride gas, and the hydrogen chloride tail gas generated in the distillation tower also directly enters the three-stage falling film abso...

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Abstract

The invention discloses an on-line purification method for hydrochloric acid in the process of producing potassium sulfate by Mannheim method. The gas from the Mannheim furnace is cooled by a cooler, and then enters a first-stage washing tower, a second-stage washing tower, and a third-stage cooling tower in sequence. The membrane absorption tower and the fourth-stage washing tower are emptied; the washing liquid obtained after washing and absorbing the environmental protection tail gas with deionized water enters the second-stage washing tower and the first-stage washing tower for washing in turn, and finally hydrochloric acid B is obtained, and the hydrochloric acid B enters the distillation tower. Distillation is carried out, the distilled fraction is cooled to obtain food-grade hydrochloric acid, deionized water washes the hydrogen chloride gas in the four-stage washing tower, and enters the three-stage falling film absorption tower to absorb the hydrogen chloride gas, and the distilled gas from the distillation tower enters the third-stage The falling film absorption tower absorbs hydrochloric acid A; the heat required by the distillation tower is provided by the exhaust gas generated by the combustion chamber that provides heat for the Mannheim furnace. The method utilizes the residual heat of the exhaust gas of the combustion chamber to perform on-line distillation and purification on the hydrochloric acid to obtain food-grade hydrochloric acid.

Description

technical field [0001] The invention belongs to the field of chemical industry, and in particular relates to an on-line purification method of hydrochloric acid in the process of producing potassium sulfate by Mannheim method. Background technique [0002] The production of potassium sulfate by the Mannheim method is to use sulfuric acid and potassium chloride in the Mannheim furnace to react under high temperature conditions to produce potassium sulfate and generate hydrogen chloride. The hydrogen chloride is absorbed by water to produce hydrochloric acid, and the potassium sulfate is cooled. The Mannheim method is by far the most mature and reliable method for producing potassium sulfate with the most stable quality. [0003] However, because the hydrogen chloride gas produced by the Mannheim method contains a small amount of impurities such as water vapor, sulfuric acid gas, potassium sulfate dust, potassium chloride dust, these impurities and hydrogen chloride gas exist ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B7/07C01D5/06C01D5/02
CPCC01B7/0712C01D5/06C01D5/02Y02P20/129
Inventor 廖全斌胡卫民黄年玉梁立军韩光金毛栋梁
Owner CHINA THREE GORGES UNIV
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