CN215249553U - Hydrochloric acid clean system - Google Patents
Hydrochloric acid clean system Download PDFInfo
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- CN215249553U CN215249553U CN202121958508.4U CN202121958508U CN215249553U CN 215249553 U CN215249553 U CN 215249553U CN 202121958508 U CN202121958508 U CN 202121958508U CN 215249553 U CN215249553 U CN 215249553U
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- hydrochloric acid
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- deironing
- dechlorination
- chlorine
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Abstract
The utility model discloses a hydrochloric acid purification system, which comprises a dechlorination device, an iron removal device and a recovery tank which are connected in sequence; the dechlorination device comprises a dechlorination tank body, activated carbon is filled in the dechlorination tank body, a dechlorination liquid inlet and a dechlorination liquid outlet are respectively arranged at the top and the bottom of the dechlorination tank body, and the dechlorination liquid inlet is used for introducing hydrochloric acid into the dechlorination tank body; the deironing device comprises a deironing tank body, resin is filled in the deironing tank body, a deironing liquid inlet and a deironing liquid outlet are respectively arranged at the top and the bottom of the deironing tank body, the deironing liquid inlet and the dechlorination liquid outlet are connected through a pipeline, and a first filter is arranged on the pipeline; the recovery tank is connected with the iron removal liquid outlet through a pipeline, and a second filter is arranged on the pipeline. The system can effectively remove free chlorine and iron under the condition of not obviously reducing the concentration of hydrochloric acid.
Description
Technical Field
The utility model relates to a waste gas treatment technical field, concretely relates to hydrochloric acid clean system.
Background
At present, the main method for treating chlorine-containing organic waste is a thermal decomposition technology, including incineration, cracking, gasification and other technologies, and the technology can reduce, harmlessly and recycle pollutants in a short time. By incineration, the highly toxic chlorine-containing organic waste decomposes inorganic substances such as carbon dioxide, water, hydrogen chloride, chlorine gas and a small amount of nitrogen oxides.
If HCl in incineration flue gas is directly discharged without being treated, the environment can be seriously polluted, and the HCl is not recycled, which is a waste of resources. The alkali liquor is adopted to directly absorb HCl, and although the alkali consumption is low and the cost is low, secondary pollution to the environment can be caused. HCl is easy to dissolve in water, water can be used as an absorbent, HCl dry gas is converted into hydrochloric acid solution with a certain concentration, the purpose of resource recovery can be achieved, and certain economic benefits are brought to enterprises. However, hydrochloric acid recovered by this method is poor in quality, contains impurities such as free chlorine and iron ions, wherein the free chlorine is yellow green toxic simple substance gas, is difficult to dissolve in water and has suffocating odor, and the chlorine gas in the air is required to be not more than 0.001mg/L in a common operation place.
A hydrochloric acid purification method in an HCl recovery unit in incineration flue gas has not been reported in systematic research at home and abroad.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a hydrochloric acid clean system, this system can be under the condition of not obviously reducing hydrochloric acid concentration, effectively detach free chlorine and iron, have good decoloration effect simultaneously.
The utility model discloses a following technical scheme realizes:
a hydrochloric acid purification system comprises a dechlorination device, an iron removal device and a recovery tank which are connected in sequence;
the dechlorination device comprises a dechlorination tank body, activated carbon is filled in the dechlorination tank body, a dechlorination liquid inlet and a dechlorination liquid outlet are respectively arranged at the top and the bottom of the dechlorination tank body, and the dechlorination liquid inlet is used for introducing hydrochloric acid into the dechlorination tank body;
the deironing device comprises a deironing tank body, resin is filled in the deironing tank body, a deironing liquid inlet and a deironing liquid outlet are respectively arranged at the top and the bottom of the deironing tank body, the deironing liquid inlet and the dechlorination liquid outlet are connected through a pipeline, and a first filter is arranged on the pipeline;
the recovery tank is connected with the iron removal liquid outlet through a pipeline, and a second filter is arranged on the pipeline.
The chlorine-containing waste is incinerated to generate hydrogen chloride gas, and the hydrogen chloride gas is absorbed by water in the absorption tower to form byproduct hydrochloric acid, but because the impurities such as simple substance chlorine, iron and the like in the incineration flue gas, besides the hydrogen chloride gas, enter the byproduct hydrochloric acid along with the absorption process of the hydrogen chloride, the application range of the byproduct hydrochloric acid is limited.
At present, the methods for removing free chlorine in waste hydrochloric acid mainly comprise a physical removal method and a chemical removal method, wherein the physical method comprises an air blowing removal method, a vacuum method and an activated carbon adsorption method, and the chemical method comprises a sodium sulfite removal method and a hydrogen peroxide removal method. Wherein, the air stripping method has the advantages of simple process, high efficiency and the like, if the waste hydrochloric acid contains CO and CO2Other gases such as NOx, etc. will also be accompanied by airThe gas escapes and is removed together, but the process has tail gas emission and needs to collect and treat the tail gas. The vacuum method has high equipment requirement and great operation difficulty, and a tail gas absorption tower is also required to be arranged for treating the tail gas. In the sodium sulfite removing method, not only SO is generated due to side reaction2Contaminating the gas and also introducing new impurity ions into the hydrochloric acid. The method for removing the free chlorine in the hydrochloric acid by using the hydrogen peroxide has good removal effect and no new impurities, but the amount of the hydrogen peroxide is not easy to control in the actual operation process and the operation difficulty is high.
The invention utilizes the porous structure of the active carbon to adsorb hydrogen chloride in a trace way and adsorb free chlorine in hydrochloric acid in a large quantity, and effectively removes the free chlorine in the hydrochloric acid on the premise of ensuring that the concentration of the hydrochloric acid is not obviously reduced. The outlet free chlorine concentration may be less than 0.0001%.
At present, the acid pickling waste liquid recycling treatment technology adopts methods such as a high-temperature roasting method, an evaporation method, an ion exchange method, a membrane treatment method (including an electrodialysis method, a nanofiltration method, an electrolysis method and the like), a chemical conversion method and the like to remove iron in hydrochloric acid. The high-temperature roasting method has the advantages of large treatment capacity, compact treatment equipment and the like, but the process has high requirements on design, management and control level and corrosion resistance of the equipment, and has high energy consumption; the evaporation method achieves the aim of indirectly removing iron by recovering hydrochloric acid, but the method has higher risk and equipment is easy to be blocked due to the influence of evaporation crystallization; the membrane treatment method has no phase change process, saves cost and has higher economic value, but the current domestic membrane mainly depends on import, has higher cost, is easy to be polluted and has limited application.
The utility model can use Fe as iron ion in hydrochloric acid according to the chemical property of iron compound2+、Fe3+、FeCl4-Three forms exist, mainly Fe according to the concentration of hydrochloric acid3+、FeCl4-Two forms exist. Removing iron ions by using resin; the iron removal efficiency of resin adsorption can reach more than 95%.
To sum up, the system dechlorination unit adopts the activated carbon adsorption method, utilizes activated carbon porous structure, and the trace adsorbs the chlorine hydride, adsorbs the free chlorine in the hydrochloric acid in a large number, and the activated carbon adsorption method has effectual, easy operation, no accessory substance and advantage such as reuse. The system iron removing unit adopts an ion exchange method, ion exchange is carried out between functional groups on ion exchange resin and iron ions in the solution, so that the iron ions in the solution are transferred to the resin, then the iron ions are separated in an elution mode, the purpose of removing the iron ions is achieved, and the eluted resin recovers the adsorption capacity for recycling. The ion exchange resin method has the advantages of strong processing capacity, no toxicity or harm, repeated cyclic recycling, low equipment investment cost, long service life and the like.
Furthermore, the height-diameter ratio of the active carbon filling in the chlorine removal tank body is more than or equal to 1.
The height-diameter ratio is the ratio of the filling height to the diameter, and the chlorine removal effect can be effectively improved by reasonably designing the height-diameter ratio of the filling of the activated carbon.
Furthermore, the height-diameter ratio of the active carbon filling in the chlorine removal tank body is more than or equal to 7.5.
Furthermore, the activated carbon is coconut shell or coal granular activated carbon with the grain diameter of 0.3-1.4 mm.
Further, the height-diameter ratio of resin filling in the iron removing tank body is more than or equal to 1.
Furthermore, the height-diameter ratio of resin filling in the iron removing tank body is more than or equal to 7.5.
Further, the resin is ionic resin or chelating resin with the particle size of 0.3-1.25 mm.
Further, the chlorine removal device is provided with a positive blowing system and a back flushing system.
The forward blowing system comprises an air inlet and an air outlet which are arranged at the top and the bottom of the chlorine removal device, and the back washing system comprises a liquid outlet and a liquid inlet which are arranged at the top and the bottom of the chlorine removal device.
When the activated carbon in the chlorine removal device is saturated in adsorption, firstly, air is adopted for forward blowing to remove redundant hydrochloric acid; then, backwashing by using desalted water with the hydrochloric acid feeding flow rate being 1-3 times, so that the activated carbon is rearranged while being regenerated, and the resistance is reduced; and finally, positively blowing air to remove redundant desalted water.
Further, a positive blowing system, a positive flushing system and a back flushing system are arranged on the iron removing device.
The positive flushing system comprises a liquid inlet and a liquid outlet which are arranged at the top and the bottom of the iron removing device, and the liquid inlet and the liquid outlet directions of the positive flushing system and the back flushing system are opposite.
After the resin in the iron removal device is adsorbed and saturated, air is firstly adopted for forward blowing to remove redundant hydrochloric acid; then, carrying out forward flushing by adopting 1-2 BV/h of desalted water, carrying out regeneration treatment on the resin, and carrying out back flushing by adopting 1-2 BV/h of desalted water; and finally, positively blowing air to remove redundant desalted water.
Further, a chlorine removal device and an iron removal device are respectively arranged on the support, and the chlorine removal device, the iron removal device and the recovery tank are of skid-mounted structures.
Compared with the prior art, the utility model, following advantage and beneficial effect have:
1. the method can effectively remove free chlorine under the condition of not obviously reducing the concentration of hydrochloric acid, and can achieve the condition that the free chlorine in the export hydrochloric acid is lower than 0.0001 percent and is far lower than the standard of superior products in the national current industrial hydrochloric acid.
2. The method can effectively remove iron ions under the condition of not obviously reducing the concentration of hydrochloric acid, and the removal rate can reach 95%.
3. The method adopts the activated carbon to remove chlorine, can remove free chlorine in the waste hydrochloric acid, has low cost, and can recycle the activated carbon.
4. The invention adopts the ion resin to realize iron removal by an ion exchange method, and has the advantages of strong processing capacity, no toxicity, repeated cyclic recycling, low equipment investment cost, long service life and the like.
5. The invention fills the blank of waste hydrochloric acid purification technology for waste incineration recovery, solves the problem of iron and free chlorine in the waste hydrochloric acid, and achieves the purpose of resource recycling.
Drawings
The accompanying drawings, which are included to provide a further understanding of the embodiments of the invention and are incorporated in and constitute a part of this application, illustrate embodiment(s) of the invention and together with the description serve to explain the principles of the invention. In the drawings:
FIG. 1 is a schematic diagram of the acid purification system.
Reference numbers and corresponding part names in the drawings:
1-a dechlorination device, 2-an iron removal device, 3-a recovery tank, 4-a first filter, 5-a second filter, 11-a dechlorination tank body, 12-a dechlorination liquid inlet, 13-a dechlorination liquid outlet, 21-an iron removal tank body, 22-an iron removal liquid inlet and 23-an iron removal liquid outlet.
Detailed Description
To make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described in detail below with reference to the following examples and drawings, and the exemplary embodiments and descriptions thereof of the present invention are only used for explaining the present invention, and are not intended as limitations of the present invention.
Example 1:
as shown in fig. 1, a hydrochloric acid purification system comprises a dechlorination device 1, an iron removal device 2 and a recovery tank 3 which are connected in sequence;
the dechlorination device 1 comprises a dechlorination tank body 11, activated carbon is filled in the dechlorination tank body 11, a dechlorination liquid inlet 12 and a dechlorination liquid outlet 13 are respectively arranged at the top and the bottom of the dechlorination tank body 11, and the dechlorination liquid inlet 12 is used for introducing hydrochloric acid into the dechlorination tank body 11;
the deironing device 2 comprises a deironing tank body 21, the deironing tank body 21 is filled with resin, a deironing liquid inlet 22 and a deironing liquid outlet 23 are respectively arranged at the top and the bottom of the deironing tank body 21, the deironing liquid inlet 22 is connected with the dechlorination liquid outlet 13 through a pipeline, a first filter 4 is arranged on the pipeline,
the recovery tank 3 is connected with an iron removal liquid outlet 23 through a pipeline, and a second filter 5 is arranged on the pipeline.
In this example, the activated carbon is coconut shell particle activated carbon with a particle size of 0.3-1.4mm, and the resin is ionic resin with a particle size of 0.3-1.25 mm.
In this example, the aspect ratio of the activated carbon filling in the chlorine removal tank 11 was 7.5, and the aspect ratio of the resin filling in the iron removal tank 21 was 7.5.
In this embodiment, the chlorine removal device 1 is provided with a forward blowing system and a back flushing system, and the active carbon is recycled through the forward blowing system and the back flushing system.
In this embodiment, the iron removing device 2 is provided with a forward blowing system, a forward flushing system and a back flushing system. The resin is recovered and utilized through the forward blowing system, the forward flushing system and the back flushing system.
In this embodiment, the chlorine removal device 1 and the iron removal device 2 are respectively mounted on a support, and the chlorine removal device 1, the iron removal device 2 and the recovery tank 3 are of a skid-mounted structure.
Hydrochloric acid solution with the concentration of 20 percent, the concentration of free chlorine of 0.0030 percent and the concentration of iron ions of 15.38mg/L enters a purification system from a dechlorination liquid inlet 12 and is sequentially subjected to dechlorination and iron removal, the concentration of outlet hydrochloric acid is 20 percent, the concentration of free chlorine is 0.0001 percent and the concentration of iron ions is 1.62 mg/L.
The above-mentioned embodiments, further detailed description of the objects, technical solutions and advantages of the present invention, it should be understood that the above description is only the embodiments of the present invention, and is not intended to limit the scope of the present invention, and any modifications, equivalent substitutions, improvements, etc. made within the spirit and principle of the present invention should be included in the scope of the present invention.
Claims (10)
1. A hydrochloric acid purification system is characterized by comprising a chlorine removal device (1), an iron removal device (2) and a recovery tank (3) which are connected in sequence;
the chlorine removal device (1) comprises a chlorine removal tank body (11), activated carbon is filled in the chlorine removal tank body (11), a chlorine removal liquid inlet (12) and a chlorine removal liquid outlet (13) are respectively formed in the top and the bottom of the chlorine removal tank body (11), and the chlorine removal liquid inlet (12) is used for introducing hydrochloric acid into the chlorine removal tank body (11);
the deironing device (2) comprises a deironing tank body (21), the deironing tank body (21) is filled with resin, a deironing liquid inlet (22) and a deironing liquid outlet (23) are respectively arranged at the top and the bottom of the deironing tank body (21), the deironing liquid inlet (22) is connected with the dechlorination liquid outlet (13) through a pipeline, and a first filter (4) is arranged on the pipeline;
the recovery tank (3) is connected with the iron removal liquid outlet (23) through a pipeline, and a second filter (5) is arranged on the pipeline.
2. The hydrochloric acid purification system according to claim 1, wherein the height-diameter ratio of the activated carbon filling in the chlorine removal tank body (11) is greater than or equal to 1.
3. The hydrochloric acid purification system as claimed in claim 1, wherein the height-diameter ratio of the activated carbon filling in the chlorine removal tank body (11) is greater than or equal to 7.5.
4. The hydrochloric acid purification system of claim 1, wherein the activated carbon is coconut shell or coal-made granular activated carbon with a particle size of 0.3-1.4 mm.
5. The hydrochloric acid purification system as claimed in claim 1, wherein the aspect ratio of resin filling in the iron removal tank (21) is 1 or more.
6. The hydrochloric acid purification system as claimed in claim 1, wherein the aspect ratio of resin filling in the iron removal tank (21) is greater than or equal to 7.5.
7. The hydrochloric acid purification system according to claim 1, wherein the resin is an ionic resin or a chelating resin with a particle size of 0.3-1.25 mm.
8. The hydrochloric acid purification system as claimed in claim 1, wherein the chlorine removal device (1) is provided with a forward blowing system and a back flushing system.
9. The hydrochloric acid purification system as claimed in claim 1, wherein the iron removal device (2) is provided with a forward blowing system, a forward flushing system and a back flushing system.
10. The hydrochloric acid purification system according to any one of claims 1 to 9, wherein the chlorine removal device (1) and the iron removal device (2) are respectively mounted on a support, and the chlorine removal device (1), the iron removal device (2) and the recovery tank (3) are of skid-mounted structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121958508.4U CN215249553U (en) | 2021-08-19 | 2021-08-19 | Hydrochloric acid clean system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121958508.4U CN215249553U (en) | 2021-08-19 | 2021-08-19 | Hydrochloric acid clean system |
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| Publication Number | Publication Date |
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| CN215249553U true CN215249553U (en) | 2021-12-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202121958508.4U Active CN215249553U (en) | 2021-08-19 | 2021-08-19 | Hydrochloric acid clean system |
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| CN (1) | CN215249553U (en) |
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2021
- 2021-08-19 CN CN202121958508.4U patent/CN215249553U/en active Active
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