A system for recycling waste hydrochloric acid in iron-containing industries

A waste hydrochloric acid and recycling technology, applied in the oxidation water/sewage treatment, metallurgical waste water treatment, water/sewage treatment and other directions, can solve the problems of inconvenient operation, high pressure, not very suitable, etc., to reduce the purchase amount, reduce Cost, easy separation effect

Active Publication Date: 2020-01-14
TIANJIN VOCATIONAL INST
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Problems solved by technology

Thermal decomposition method and high temperature hydrolysis method can be divided into roasting method, fluidized bed method, etc. The working principle of these two methods is the same, both of which are to react waste hydrochloric acid containing ferrous chloride with oxygen at high temperature and absorb Concentrate volatilized hydrogen chloride, and the finished products are hydrochloric acid and iron red. The disadvantages are large investment, high operating cost, difficult technology, difficult management and maintenance
The extraction method uses an extract composed of an organic phase for countercurrent extraction, and the method of recycling the extract phase still has high investment and is inconvenient to operate, so it is not suitable
The membrane separation method uses membrane ions to selectively separate iron and acid. The disadvantage is that with the increase of the osmotic pressure of iron ions on both sides of the membrane, a large pressure energy input is required, and it has a great impact on the material and compressive performance of the membrane. High requirements are put forward, and the initial investment and operating costs are relatively high
Precipitation method is to utilize flocculant to flocculate ferrous chloride in waste hydrochloric acid. Although this method utilizes part of ferrous chloride in waste hydrochloric acid, there is still a small part of ferrous chloride in the remaining waste acid solution. This makes the purity level of the product generated by the subsequent waste acid treatment generally not high, which affects the performance of the product
The neutralization method uses alkali to react with waste hydrochloric acid. This is the oldest method for treating pickling waste liquid. However, because hydrogen chloride and ferrous chloride in waste acid liquid have not been utilized, and it is easy to cause secondary pollution, At present, this method is basically no longer used

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  • A system for recycling waste hydrochloric acid in iron-containing industries
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  • A system for recycling waste hydrochloric acid in iron-containing industries

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Embodiment Construction

[0032]The system of the present invention will be further described below in conjunction with the accompanying drawings and specific embodiments. The following embodiments are only descriptive, not restrictive, and cannot limit the protection scope of the present invention.

[0033] figure 1 It is an embodiment of the present invention. As shown in the figure, the resource treatment system for iron-containing industrial waste hydrochloric acid includes: the first deacidification tower 10, the first pickling tower 11, the first hydrogen chloride compressor 17, the first circulating acid pump 18, and the first material pump 19. Aeration reactor 12, buffer tank 13 and solid-liquid separation device.

[0034] The first deacidification tower 10 is used to carry out bubbling and stirring, under the condition of air blowing and desorption and negative pressure, the hydrogen chloride gas produced after the salting-out agent and iron-containing industrial waste hydrochloric acid are m...

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Abstract

The invention discloses a system for resourceful treatment of iron-containing industrial waste hydrochloric acid. A first acid pickling tower is used for carrying out acid pickling and concentrating on a hydrogen chloride-containing gas which escapes from a first deacidification tower and compressed by a compressor to obtain a finished product industrial hydrochloric acid; an aeration reactor is used for reacting a liquid waste of the first deacidification tower with crystal or a solution of ammonium bicarbonate, ammonium carbonate, sodium bicarbonate or sodium carbonate, generating ferrous hydroxide and ferric hydroxide and generating ammonium chloride or sodium chloride and ferric hydroxide under aeration oxidation and bubbling mixing conditions and sequentially conveying the solid-liquid mixture generated through reaction to a buffer tank and a solid-liquid separator; the buffer tank is used for removing foam, discharging separated carbon dioxide and excessive air or oxygen and separating out an ammonium chloride or sodium chloride solution; and the solid-liquid separator is used for separating out a ferric hydroxide solid product and ammonium chloride or sodium chloride crystal. The concentration of the hydrochloric acid recovered through the acid pickling tower is about 23%, about 95% of hydrochloric acid in the iron-containing waste hydrochloric acid is recovered and the purchase quantity of the hydrochloric acid is reduced.

Description

technical field [0001] The invention belongs to the field of environmental protection and relates to the treatment of industrial iron-containing waste hydrochloric acid, in particular to a system for recycling iron-containing industrial waste hydrochloric acid. Background technique [0002] As a commonly used chemical product, hydrochloric acid is widely used in carbon steel cold rolling, galvanizing and other processes. As a pickling medium, hydrochloric acid reacts with iron oxide on the surface of steel to generate ferrous chloride and ferric chloride and dissolve them in the acid solution. The hydrochloric acid waste liquid produced by this reaction contains about 5% hydrochloric acid and 10-12% ferrous chloride and ferric chloride. If this part of the iron-containing hydrochloric acid waste liquid is directly discharged, it will cause serious environmental damage to the discharge area. pollute. In addition, the waste acid liquid contains ferrous chloride and hydrogen ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B7/07C02F9/04C02F103/16C02F101/12C02F101/20
CPCC01B7/0706C02F1/00C02F1/20C02F1/72C02F9/00C02F2101/12C02F2101/203C02F2103/16
Inventor 王少杰刘炳光刘冰冰
Owner TIANJIN VOCATIONAL INST
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