CN219879510U - Hydrogen chloride washing tower - Google Patents

Hydrogen chloride washing tower Download PDF

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Publication number
CN219879510U
CN219879510U CN202321145739.2U CN202321145739U CN219879510U CN 219879510 U CN219879510 U CN 219879510U CN 202321145739 U CN202321145739 U CN 202321145739U CN 219879510 U CN219879510 U CN 219879510U
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China
Prior art keywords
hydrogen chloride
tower body
tower
washing
ceramic
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CN202321145739.2U
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Chinese (zh)
Inventor
孟会来
陈科榕
于红红
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Shaanxi Yide Taiyuan Technology Co ltd
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Shaanxi Yide Taiyuan Technology Co ltd
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Abstract

The utility model provides a hydrogen chloride washing tower, which comprises a base, a tower body arranged on the base, wherein a plurality of layers of porcelain rings are arranged in the tower body, one side of the tower body is provided with a hydrogen chloride inlet, the other side of the tower body is provided with a hydrogen chloride outlet, and the top of the tower body is provided with a spray head; the hydrogen chloride cooling tower has the characteristics of simple structure and good hydrogen chloride washing effect, and can produce byproducts when potassium sulfate is produced: the hydrogen chloride is subjected to a washing treatment so that the hydrogen chloride becomes a hydrochloric acid solution for subsequent treatment.

Description

Hydrogen chloride washing tower
Technical Field
The utility model belongs to the technical field of potassium sulfate production equipment, and particularly relates to a hydrogen chloride washing tower.
Background
The potassium sulfate is a potash fertilizer prepared by mixing natural sulfate potassium ore such as alunite and chloride and calcining and decomposing at high temperature. The chemical formula is K 2 SO 4 . Potassium content (K) 2 50% -52% of O). White diamond or hexagonal crystal is easy to dissolve in water, has small hygroscopicity, belongs to physiological acid fertilizer, and has strong quick action. After being applied to soil, potassium (K+) is dissolved in soil solution and exists in an ionic state, and can be selectively absorbed by plants or adsorbed by soil colloid. After adsorption, caSO with low solubility is formed in calcareous soil 4 Formation of H in acid soil 2 SO 4 . Thus, the acidification of the soil is less than the HCl formed after potassium chloride application. Is suitable for various soil and crops, but should be preferentially distributed to crops like tobacco, potato, grape, flax and the like which are potassium-like and chlorine-like. Can be used as base fertilizer, additional fertilizer, seed fertilizer and external root fertilizer. The application should be divided into several times on sandy soil to avoid leaching of potassium. On acid soil, the fertilizer should be applied in combination with alkaline fertilizers such as lime to prevent further acidification of the soil and influence on plant growth. The potassium sulfate is an important variety in potash fertilizer, is a high-quality fertilizer, has a saline-alkali soil index of only about 40% of that of potassium chloride, and is particularly suitable for some commercial crops such as tobacco, watermelons, tea, oranges, grapes and the like which are free of chlorine. The potassium sulfate can not only improve the crop yield, but also improve the quality of the crops, and can improve the disease resistance of the crops when used for sulfur-deficient soil.
At present, the main methods for producing potassium sulfate are as follows: man Ha Mfa, association method, double decomposition method, etc. Wherein, man Ha Mfa is a process for producing potassium sulfate by using sulfuric acid and potassium chloride as raw materials. The production method comprises the steps of carrying out the internal reaction of potassium chloride and concentrated sulfuric acid in a Man Ha Mlu, firstly, generating potassium bisulfate by the reaction, and then continuously reacting with the potassium chloride at a higher temperature to generate potassium sulfate; natural gas is utilized to supply heat in the combustion chamber of the reaction furnace, the temperature is 1000-1100 ℃, and the temperature of the reaction chamber is controlled at 520-540 ℃. Cooling, crushing and partially neutralizing the reaction product to obtain a product, and cooling, washing and absorbing a byproduct HCl to obtain hydrochloric acid with the mass fraction of 32-35%.
However, the cooling and washing treatment of byproduct HCl in the prior art still has the problem of low washing efficiency of the washing tower.
Disclosure of Invention
The utility model aims to provide a hydrogen chloride washing tower which is used for washing byproduct hydrogen chloride in the production process of potassium sulfate.
The hydrogen chloride washing tower provided by the utility model comprises a base, a tower body arranged on the base, wherein a plurality of layers of porcelain rings are arranged in the tower body, a hydrogen chloride inlet is formed in one side of the tower body, a hydrogen chloride outlet is formed in the other side of the tower body, and a spray head is arranged at the top of the tower body.
Further, the radius of the multi-layer porcelain ring is reduced from the bottom to the top of the porcelain ring layer by layer.
Further, a plurality of inward extending tongues are arranged on the inner wall of the porcelain ring.
Further, a supporting piece is arranged below the multi-layer porcelain ring.
Further, supporting legs are arranged below the tower body.
Further, the tower body is made of nickel-iron alloy.
Further, the ceramic ring is made of ceramic.
The hydrogen chloride cooling tower provided by the utility model has the characteristics of simple structure and good hydrogen chloride washing effect, and can produce byproducts when potassium sulfate is produced: washing the hydrogen chloride to change the hydrogen chloride into hydrochloric acid solution so as to carry out subsequent treatment; the ceramic pall rings are arranged in the cooling tower, so that the washing of hydrogen chloride can be more efficiently performed, and compared with a hydrogen chloride cooling mode in the prior art, the hydrochloric acid cooling efficiency of the hydrogen chloride cooling tower can be improved by more than 20%.
The utility model will now be described in detail with reference to the drawings and examples.
Drawings
Fig. 1 is a schematic diagram of the structure of a hydrogen chloride cooling tower.
Fig. 2 is a schematic top view of the porcelain ring.
In the figure: 1. a base; 2. a tower body; 3. a porcelain ring; 4. a spray head; 5. a hydrogen chloride inlet; 6. a hydrogen chloride outlet; 7. a support; 8. support legs; 9. the tongue is extended inwards.
Detailed Description
The following detailed description, structural features and functions of the present utility model are provided with reference to the accompanying drawings and examples in order to further illustrate the technical means and effects of the present utility model to achieve the predetermined objects.
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
In the description of the present utility model, it should be understood that the terms "center," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "aligned," "overlapping," "bottom," "inner," "outer," and the like indicate orientations or positional relationships based on the orientation or positional relationships shown in the drawings, merely to facilitate description of the present utility model and simplify the description, and do not indicate or imply that the devices or elements referred to must have a specific orientation, be configured and operate in a specific orientation, and therefore should not be construed as limiting the present utility model.
The terms "first," "second," and the like, are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defining "a first", "a second" may include one or more such features, either explicitly or implicitly; in the description of the present utility model, unless otherwise indicated, the meaning of "a plurality" is two or more.
Example 1
The embodiment provides a hydrogen chloride washing tower as shown in fig. 1, which comprises a base 1 and a tower body 2 arranged on the base 1, wherein a plurality of layers of porcelain rings 3 are arranged in the tower body 2, one side of the tower body 2 is provided with a hydrogen chloride inlet 5, the other side of the tower body 2 is provided with a hydrogen chloride outlet 6, and the top of the tower body 2 is provided with a spray head 4; in practical application, hydrogen chloride is washed in the tower body 2 of the tower through the hydrogen chloride inlet 5 and is dispersed in the tower body 2, and the spray head 4 sprays washing liquid from the uppermost part, so that the hydrogen chloride is dissolved in the washing liquid to form hydrochloric acid solution, and then flows out through the hydrogen chloride outlet 6; the multi-layer porcelain ring 3 can improve the washing efficiency of hydrogen chloride.
Furthermore, the radius of the multi-layer ceramic ring 3 is reduced layer by layer from bottom to top, so that the washing liquid can be more fully distributed on each part of the multi-layer ceramic ring 3 from top to bottom, and the washing efficiency of hydrogen chloride is improved.
Furthermore, the inner wall of the porcelain ring 3 is provided with a plurality of inner extending tongues 9, the number of the inner extending tongues 9 is generally 3-6, and the inner extending tongues 9 are arranged on the inner wall of the porcelain ring 3 at equal intervals, and are shown in a top view of the porcelain ring with 4 inner extending tongues in the figure 2.
Further, the support piece 7 is arranged below the ceramic ring 3 in the multiple layers, the support piece 7 supports the ceramic ring 3, and meanwhile hydrogen chloride gas can enter the ceramic ring 3 from the lower part, so that the hydrogen chloride can be more efficiently washed.
Further, support legs 8 are arranged below the tower body 2, and the support legs 8 mainly play a supporting role.
Furthermore, the tower body 2 is made of nickel-iron alloy, and the nickel-iron alloy has the characteristics of high strength, excellent heat resistance and excellent acid resistance, and is very suitable for the hydrogen chloride cooling tower.
Further, the ceramic ring 3 is a pall ring made of ceramic.
In summary, the hydrogen chloride cooling tower provided by the utility model has the characteristics of simple structure and good hydrogen chloride washing effect, and can be used for producing byproducts during potassium sulfate production: washing the hydrogen chloride to change the hydrogen chloride into hydrochloric acid solution so as to carry out subsequent treatment; the ceramic pall rings are arranged in the cooling tower, so that the washing of hydrogen chloride can be more efficiently performed, and compared with a hydrogen chloride cooling mode in the prior art, the hydrochloric acid cooling efficiency of the hydrogen chloride cooling tower can be improved by more than 20%.
The foregoing is a further detailed description of the utility model in connection with the preferred embodiments, and it is not intended that the utility model be limited to the specific embodiments described. It will be apparent to those skilled in the art that several simple deductions or substitutions may be made without departing from the spirit of the utility model, and these should be considered to be within the scope of the utility model.

Claims (7)

1. A hydrogen chloride scrubber, characterized in that: the novel ceramic tower comprises a base (1), and a tower body (2) arranged on the base (1), wherein a plurality of layers of ceramic rings (3) are arranged in the tower body (2), a hydrogen chloride inlet (5) is formed in one side of the tower body (2), a hydrogen chloride outlet (6) is formed in the other side of the tower body (2), and a spray head (4) is arranged at the top of the tower body (2).
2. A hydrogen chloride scrubber as defined in claim 1, wherein: the radius of the multi-layer porcelain ring (3) is reduced from the bottom to the top layer by layer.
3. A hydrogen chloride scrubber according to claim 1 or 2, wherein: the inner wall of the porcelain ring (3) is provided with a plurality of inward extending tongues (9).
4. A hydrogen chloride scrubber as defined in claim 1, wherein: a supporting piece (7) is arranged below the multi-layer ceramic ring (3).
5. A hydrogen chloride scrubber as defined in claim 1, wherein: support legs (8) are arranged below the tower body (2).
6. A hydrogen chloride scrubber as defined in claim 1, wherein: the tower body (2) is made of nickel-iron alloy.
7. A hydrogen chloride scrubber as defined in claim 1, wherein: the ceramic ring (3) is a pall ring made of ceramic.
CN202321145739.2U 2023-05-12 2023-05-12 Hydrogen chloride washing tower Active CN219879510U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202321145739.2U CN219879510U (en) 2023-05-12 2023-05-12 Hydrogen chloride washing tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202321145739.2U CN219879510U (en) 2023-05-12 2023-05-12 Hydrogen chloride washing tower

Publications (1)

Publication Number Publication Date
CN219879510U true CN219879510U (en) 2023-10-24

Family

ID=88411296

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202321145739.2U Active CN219879510U (en) 2023-05-12 2023-05-12 Hydrogen chloride washing tower

Country Status (1)

Country Link
CN (1) CN219879510U (en)

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