CN220940663U - Automatic temperature regulating and controlling system for ferric salt hydrolysis device containing metatitanic acid - Google Patents
Automatic temperature regulating and controlling system for ferric salt hydrolysis device containing metatitanic acid Download PDFInfo
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- CN220940663U CN220940663U CN202322737251.5U CN202322737251U CN220940663U CN 220940663 U CN220940663 U CN 220940663U CN 202322737251 U CN202322737251 U CN 202322737251U CN 220940663 U CN220940663 U CN 220940663U
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- ferric salt
- hydrolysis
- fixedly connected
- temperature
- hydrolysis kettle
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- 238000006460 hydrolysis reaction Methods 0.000 title claims abstract description 135
- 230000007062 hydrolysis Effects 0.000 title claims abstract description 132
- 150000003839 salts Chemical class 0.000 title claims abstract description 94
- 239000002253 acid Substances 0.000 title claims abstract description 26
- 230000001105 regulatory effect Effects 0.000 title abstract description 5
- 230000001276 controlling effect Effects 0.000 title description 2
- 238000003756 stirring Methods 0.000 claims abstract description 25
- 238000007790 scraping Methods 0.000 claims description 6
- 239000000523 sample Substances 0.000 claims description 3
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 239000002002 slurry Substances 0.000 abstract description 46
- 230000000694 effects Effects 0.000 abstract description 11
- 150000002505 iron Chemical class 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000011010 flushing procedure Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- -1 salt compound Chemical class 0.000 description 2
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 229910001447 ferric ion Inorganic materials 0.000 description 1
- 229960002089 ferrous chloride Drugs 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model provides an automatic temperature regulation and control system for a ferric salt hydrolysis device containing metatitanic acid, which relates to the technical field of ferric salt hydrolysis devices containing metatitanic acid, and comprises the following components: and (5) mounting a frame. When the temperature detector detects that the temperature of the ferric salt slurry is too low, the ferric salt slurry is started through the electric connection with the electronic valve, high-temperature steam enters the hydrolysis kettle along with the air inlet pipe and warms the ferric salt slurry, the stirring device is driven by the motor to stir the ferric salt slurry and the high-temperature steam, so that the ferric salt slurry is heated uniformly, the temperature of the ferric salt slurry is raised to a set value by the high-temperature steam, when the temperature detector detects that the temperature of the ferric salt slurry is higher than the set value, the opening of the electronic valve is regulated until the ferric salt slurry is closed, and when the temperature of the ferric salt slurry is lower than the set value, the opening of the electronic valve is opened, so that automatic temperature regulation is realized, and the automatic temperature regulation effect of the ferric salt hydrolysis device containing the meta-titanic acid is improved.
Description
Technical Field
The utility model relates to the technical field of ferric salt hydrolysis devices containing metatitanic acid, in particular to an automatic temperature regulation and control system for a ferric salt hydrolysis device containing metatitanic acid.
Background
Ferric salt refers to a salt compound containing ferric ions, and ferrous sulfate, ferric sulfate, ferrous chloride and the like are common, when ferric salt is dissolved in water, hydrolysis reaction occurs to generate hydroxyl ions, and hydrolysis reaction refers to a substance dissolved in water and who takes charge of reacting to generate new substances.
In the production process, ferric salt can be dissolved into ferric salt slurry by adding meta-titanic acid into production raw materials in advance by using a dissolving device, then the ferric salt slurry enters a hydrolysis kettle to carry out hydrolysis reaction, the temperature of the ferric salt slurry needs to be controlled in the hydrolysis process of the ferric salt, a temperature display device arranged on the surface of the hydrolysis kettle is usually observed manually, high-temperature steam is input into the hydrolysis kettle according to personal experience, but the temperature in the hydrolysis kettle is controlled manually, personnel is required to continuously observe the temperature in the hydrolysis kettle in the hydrolysis process of the ferric salt, and a long time is usually required in the hydrolysis process of the ferric salt, so that the working intensity of the personnel is increased.
Disclosure of utility model
The utility model aims to solve the problems that in the prior art, personnel are required to continuously observe the temperature in a hydrolysis kettle in the ferric salt hydrolysis process, and the working strength of personnel is increased in the ferric salt hydrolysis process generally, and provides an automatic temperature regulation and control system for a ferric salt hydrolysis device containing metatitanic acid.
In order to achieve the above purpose, the present utility model adopts the following technical scheme: an automatic temperature regulation and control system for a ferric salt hydrolysis device containing metatitanic acid, comprising: the inner surface wall of the mounting frame is fixedly connected with a first hydrolysis assembly, and a second hydrolysis assembly is fixedly connected to one side of the inner surface wall of the mounting frame, which is far away from the first hydrolysis assembly; the first hydrolysis assembly, the first hydrolysis assembly includes first hydrolysis kettle, the surface of first hydrolysis kettle and the interior table wall fixed connection of mounting bracket, the up end fixedly connected with first motor of first hydrolysis kettle, the up end of first motor rotates the up end that runs through first hydrolysis kettle, the output fixedly connected with first dwang of first motor, the surface fixedly connected with first connecting block of first dwang, the both sides surface equidistance of first connecting block is provided with a plurality of first stirring leaves respectively, the internal surface symmetry of first hydrolysis kettle is provided with temperature probe, the up end of first hydrolysis kettle is close to one side position of first motor and is provided with the molysite inlet pipe, the lower terminal surface of first hydrolysis kettle is provided with the intake pipe, the up end of intake pipe is provided with the check valve, the intake pipe is the intercommunication setting with the check valve, the surface of intake pipe is provided with electronic valve.
Preferably, the second hydrolysis assembly comprises a second hydrolysis kettle, the surface of the second hydrolysis kettle is fixedly connected with the inner surface wall of the mounting frame, the upper end face of the second hydrolysis kettle is fixedly connected with a second motor, the output end of the second motor is connected with the upper end face penetrating through the second hydrolysis kettle, the output end of the second motor is fixedly connected with a second rotating rod, the outer surface of the second rotating rod is fixedly connected with a second connecting block, a plurality of second stirring blades are respectively and equidistantly arranged on the outer surfaces of two sides of the second connecting block, the outer surface of the second hydrolysis kettle is fixedly connected with a connecting pipe, the left end face of the connecting pipe is fixedly connected with the outer surface of the first hydrolysis kettle, and the first hydrolysis kettle and the second hydrolysis kettle are communicated through the connecting pipe.
Preferably, first scrapers are symmetrically arranged on the outer surfaces of the two sides of the first connecting block, and the outer surfaces of the first scrapers are rotationally connected with the inner surface of the first hydrolysis kettle.
Preferably, the inner bottom surface of the first hydrolysis kettle is fixedly connected with a first bearing column, and the inner surface wall of the first bearing column is rotationally connected with the lower end surface of the first rotating rod.
Preferably, the outer surfaces of the ferric salt feeding pipe and the air inlet pipe penetrate through the upper end surface and the lower end surface of the first hydrolysis kettle respectively, and the outer surfaces of the ferric salt feeding pipe and the air inlet pipe are fixedly connected with the inner surface wall of the first hydrolysis kettle respectively.
Preferably, second scrapers are symmetrically arranged on the outer surfaces of two sides of the second connecting block, and the outer surfaces of the second scrapers are rotationally connected with the inner surface of the second hydrolysis kettle.
Preferably, the inner bottom surface of the second hydrolysis kettle is fixedly connected with a second bearing column, and the inner surface wall of the second bearing column is rotationally connected with the lower end surface of the second rotating rod.
Compared with the prior art, the utility model has the advantages and positive effects that,
1. When the temperature detector detects that the temperature of the ferric salt slurry is too low, the ferric salt slurry is started through the electric connection with the electronic valve, high-temperature steam enters the hydrolysis kettle along with the air inlet pipe and warms the ferric salt slurry, the stirring device is driven by the motor to stir the ferric salt slurry and the high-temperature steam, so that the ferric salt slurry is heated uniformly, the temperature of the ferric salt slurry is raised to a set value by the high-temperature steam, when the temperature detector detects that the temperature of the ferric salt slurry is higher than the set value, the opening of the electronic valve is regulated until the ferric salt slurry is closed, and when the temperature of the ferric salt slurry is lower than the set value, the opening of the electronic valve is opened, so that automatic temperature regulation is realized, and the automatic temperature regulation effect of the ferric salt hydrolysis device containing the meta-titanic acid is improved.
2. According to the utility model, when the iron salt water hydrolysis device is used, the first scraping plate and the second scraping plate are respectively arranged on the outer surfaces of the first connecting block and the second connecting block, so that when the stirring device stirs the iron salt slurry, the outer surfaces of the first scraping plate and the second scraping plate are respectively scraped with the inner surfaces of the first hydrolysis kettle and the second hydrolysis kettle, the iron salt slurry or solid matters are prevented from being adhered to the hydrolysis kettles, and the reaction effect of the iron salt water hydrolysis device is improved.
Drawings
FIG. 1 is a perspective view of an automatic temperature control system for a ferric salt hydrolysis device containing metatitanic acid;
FIG. 2 is a schematic diagram showing the structure of a first hydrolysis assembly of an automatic temperature control system for a ferric salt hydrolysis apparatus containing metatitanic acid;
FIG. 3 is a schematic diagram showing the structure of a second hydrolysis assembly of the automatic temperature control system for a ferric salt hydrolysis apparatus containing metatitanic acid;
Fig. 4 is a schematic diagram of a part of a temperature automatic control system for a ferric salt hydrolysis device containing metatitanic acid according to the present utility model.
Legend description: 1. a mounting frame; 2. a first hydrolysis assembly; 201. a first hydrolysis tank; 202. a first motor; 203. an iron salt feeding pipe; 205. a first rotating lever; 206. a first connection block; 207. a first stirring blade; 208. a first scraper; 209. a one-way valve; 210. an air inlet pipe; 211. an electronic valve; 212. a first load-bearing column; 213. a temperature detector; 3. a second hydrolysis assembly; 301. a second hydrolysis tank; 302. a second motor; 303. a second rotating lever; 304. a second connection block; 305. a second stirring blade; 306. a second scraper; 307. a second load-bearing column; 308. and (5) connecting pipes.
Detailed Description
In order that the above objects, features and advantages of the utility model will be more clearly understood, a further description of the utility model will be rendered by reference to the appended drawings and examples. It should be noted that, without conflict, the embodiments of the present utility model and features in the embodiments may be combined with each other.
In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present utility model, but the present utility model may be practiced otherwise than as described herein, and therefore the present utility model is not limited to the specific embodiments of the disclosure that follow.
Embodiment 1 as shown in fig. 1 to 4, the present utility model provides an automatic temperature control system for a ferric salt hydrolysis device containing metatitanic acid, comprising: the device comprises a mounting frame 1, wherein a first hydrolysis assembly 2 is fixedly connected to the inner surface wall of the mounting frame 1, and a second hydrolysis assembly 3 is fixedly connected to the inner surface wall of the mounting frame 1 at a position away from the first hydrolysis assembly 2; the first hydrolysis assembly 2, the first hydrolysis assembly 2 includes first hydrolysis kettle 201, the surface of first hydrolysis kettle 201 and the interior surface wall fixed connection of mounting bracket 1, the up end fixedly connected with first motor 202 of first hydrolysis kettle 201, the up end of first motor 202 rotates and runs through the up end of first hydrolysis kettle 201, the output of first motor 202 fixedly connected with first dwang 205, the surface fixedly connected with first connecting block 206 of first dwang 205, the both sides surface of first connecting block 206 equidistance is provided with a plurality of first stirring leaves 207 respectively, the internal surface symmetry of first hydrolysis kettle 201 is provided with temperature probe 213, the up end of first hydrolysis kettle 201 is close to one side position of first motor 202 and is provided with molysite inlet tube 203, the lower terminal surface of first hydrolysis kettle 201 is provided with intake pipe 210, the up end of intake pipe 210 is provided with the check valve 209, intake pipe 210 is the intercommunication setting with the check valve 209, the surface of intake pipe 210 is provided with electronic valve 211. The second hydrolysis assembly 3 includes second hydrolysis tank 301, the surface of second hydrolysis tank 301 and the interior surface wall fixed connection of mounting bracket 1, the up end fixedly connected with second motor 302 of second hydrolysis tank 301, the output of second motor 302 is tied to and is rotated the up end that runs through second hydrolysis tank 301, the output fixedly connected with second dwang 303 of second motor 302, the surface fixedly connected with second connecting block 304 of second dwang 303, the both sides surface of second connecting block 304 equidistance is provided with a plurality of second stirring leaf 305 respectively, the surface fixedly connected with connecting pipe 308 of second hydrolysis tank 301, the left end face of connecting pipe 308 and the surface fixedly connected of first hydrolysis tank 201, first hydrolysis tank 201 and second hydrolysis tank 301 pass through connecting pipe 308 intercommunication.
The effect achieved in the whole embodiment 1 is that when the automatic temperature regulation and control system for the ferric salt hydrolysis device containing the metatitanic acid is used, firstly, the device is integrally placed at a proper working place through a mounting frame 1, then a ferric salt feeding pipe 203 is connected with an external conveying pipe, ferric salt slurry containing the metatitanic acid enters a first hydrolysis kettle 201 from the ferric salt feeding pipe 203, when the ferric salt slurry is added to 2/3 of the first hydrolysis kettle 201, conveying is stopped, the temperature of the initially-entered ferric salt slurry is low, the reaction is not favored, a temperature detector 213 can open the electronic valve 211 through the electric connection function with the electronic valve 211, external high-temperature steam enters a one-way valve 209 through an air inlet pipe 210, the ferric salt slurry in the first hydrolysis kettle 201 is washed, the high-temperature steam moves from bottom to top in the ferric salt slurry, a first motor 202 is synchronously started, the output end of the first motor 202 drives the first rotating rod 205 to correspondingly rotate in the first bearing column 212, so that the first stirring blades 207 symmetrically arranged on the surface of the first stirring rod can uniformly stir the ferric salt slurry, high-temperature steam sprayed from bottom to top can uniformly contact with the ferric salt slurry and heat the ferric salt slurry, the heating effect on the ferric salt slurry is improved, part of ferric salt slurry overflows outwards due to the stirring of the plurality of first stirring blades 207 and the impact force generated by the high-temperature gas, part of the ferric salt slurry enters the second hydrolysis kettle 301 through the connecting pipe 308 arranged at the overflow position, part of the high-temperature steam enters the second hydrolysis kettle 301 through the connecting pipe 308 to heat the overflowed ferric salt slurry, the second motor 302 is started, the output end of the second motor 302 drives the second rotating rod 303 to correspondingly rotate in the second bearing column 307, the second connecting block 304 can be made to drive a plurality of second stirring blades 305 arranged on two sides of the second connecting block to stir overflowed ferric salt slurry and contact with high-temperature steam to raise the surface temperature, the input of the high-temperature steam is controlled through the electric connection effect of the temperature detector 213 and the electronic valve 211, the temperature of the ferric salt slurry is raised to a set value by utilizing the high-temperature steam, the electronic valve 211 can be correspondingly adjusted, the opening of the electronic valve can be adjusted, and the automatic temperature regulation and control effect of the ferric salt hydrolysis device containing the metatitanic acid is improved.
In embodiment 2, as shown in fig. 1 to 4, first scrapers 208 are symmetrically disposed on both outer surfaces of the first connecting block 206, and the outer surface of the first scraper 208 is rotatably connected to the inner surface of the first hydrolysis tank 201. The inner bottom surface of the first hydrolysis kettle 201 is fixedly connected with a first bearing column 212, and the inner surface wall of the first bearing column 212 is rotationally connected with the lower end surface of the first rotating rod 205. The outer surfaces of the ferric salt feeding pipe 203 and the air inlet pipe 210 respectively penetrate through the upper end surface and the lower end surface of the first hydrolysis kettle 201, and the outer surfaces of the ferric salt feeding pipe 203 and the air inlet pipe 210 are respectively fixedly connected with the inner surface wall of the first hydrolysis kettle 201. Second scrapers 306 are symmetrically arranged on the outer surfaces of two sides of the second connecting block 304, and the outer surfaces of the second scrapers 306 are rotationally connected with the inner surface of the second hydrolysis kettle 301. The inner bottom surface of the second hydrolysis tank 301 is fixedly connected with a second bearing column 307, and the inner surface wall of the second bearing column 307 is rotationally connected with the lower end surface of the second rotating rod 303.
The effect that its whole embodiment 2 reached is, when using, through set up first scraper blade 208 and second scraper blade 306 respectively at the surface of first connecting block 206 and second connecting block 304, can make corresponding motor when driving corresponding stirring leaf, the surface of first scraper blade 208 and second scraper blade 306 can strike off at the internal surface of first hydrolysis tank 201 and second hydrolysis tank 301 respectively, strike off the ferric salt ground paste or the solid product of adhesion on the inner wall, avoid gluing the ferric salt ground paste of adhesion on the inner wall and can not carry out even heating with high temperature steam, improved the hydrolysis effect to the ferric salt that contains the metatitanic acid.
Working principle: when the automatic temperature regulation and control system for the ferric salt hydrolysis device containing the metatitanic acid is used, the ferric salt slurry containing the metatitanic acid enters the first hydrolysis kettle 201 from the ferric salt feeding pipe 203, the ferric salt slurry can be added to the 2/3 part of the first hydrolysis kettle 201, the temperature of the ferric salt slurry which is initially entered is low and is unfavorable for reaction, the temperature detector 213 can enable a detection result to be in contact with the ferric salt through the electric connection function of the electronic valve 211, the electronic valve 211 is opened, external high-temperature steam enters the one-way valve 209 through the air inlet pipe 210 and is subjected to flushing temperature to the ferric salt slurry in the first hydrolysis kettle 201, the high-temperature steam can move from bottom to top in the ferric salt slurry, the first motor 202 is synchronously started, the output end of the first motor 202 drives the first rotary rod 205 to correspondingly rotate in the first bearing column 212, the first stirring blade 207 which is symmetrically arranged on the surface of the first rotary rod can enable the first stirring blade to uniformly stir the ferric salt slurry, the high-temperature steam which is ejected from bottom to be in contact with the ferric salt slurry, the high-temperature steam which is uniformly to be in contact with the ferric salt slurry, the effect of flushing temperature is improved, the effect of the ferric salt slurry is achieved through the electric connection function of the electronic valve 211, the high-temperature steam is electrically connected with the electronic valve 211, the high-temperature steam is correspondingly regulated and the ferric salt vapor, and the automatic temperature regulation and controlled by the ferric salt temperature regulation device is adjusted to the ferric salt temperature.
The present utility model is not limited to the above-mentioned embodiments, and any equivalent embodiments which can be changed or modified by the technical content disclosed above can be applied to other fields, but any simple modification, equivalent changes and modification made to the above-mentioned embodiments according to the technical substance of the present utility model will still fall within the protection scope of the technical solution of the present utility model.
Claims (7)
1. An automatic temperature regulation and control system for a ferric salt hydrolysis device containing metatitanic acid, which is characterized by comprising: the device comprises a mounting frame (1), wherein a first hydrolysis assembly (2) is fixedly connected to the inner surface wall of the mounting frame (1), and a second hydrolysis assembly (3) is fixedly connected to the inner surface wall of the mounting frame (1) at a position far away from the first hydrolysis assembly (2);
The first subassembly (2) that hydrolyzes, first subassembly (2) that hydrolyzes includes first cauldron (201) that hydrolyzes, the surface of first cauldron (201) that hydrolyzes and the interior table wall fixed connection of mounting bracket (1), the up end fixedly connected with first motor (202) of first cauldron (201), the output of first motor (202) rotates the up end that runs through first cauldron (201) that hydrolyzes, the output fixedly connected with first dwang (205) of first motor (202), the surface fixedly connected with first connecting block (206) of first dwang (205), the both sides surface equidistance respectively is provided with a plurality of first stirring leaf (207) of first connecting block (206), the internal surface symmetry of first cauldron (201) that hydrolyzes is provided with temperature probe (213), the up end of first cauldron (201) is close to one side position of first motor (202) is provided with ferric salt (203), the lower terminal surface of first cauldron (201) that hydrolyzes is provided with intake pipe (210), the up end (210) are provided with intake pipe (209), intake pipe (209) are provided with one-way valve (209).
2. The automatic temperature control system for a ferric salt hydrolysis device containing metatitanic acid according to claim 1, wherein: the second hydrolysis assembly (3) comprises a second hydrolysis kettle (301), the outer surface of the second hydrolysis kettle (301) is fixedly connected with the inner surface wall of the mounting frame (1), the upper end face of the second hydrolysis kettle (301) is fixedly connected with a second motor (302), the output end of the second motor (302) is turned to the upper end face penetrating the second hydrolysis kettle (301), the output end of the second motor (302) is fixedly connected with a second rotating rod (303), the outer surface of the second rotating rod (303) is fixedly connected with a second connecting block (304), a plurality of second stirring blades (305) are respectively arranged on the outer surfaces of two sides of the second connecting block (304) at equal intervals, the outer surface of the second hydrolysis kettle (301) is fixedly connected with a connecting pipe (308), the left end face of the connecting pipe (308) is fixedly connected with the outer surface of the first hydrolysis kettle (201), and the first hydrolysis kettle (201) and the second hydrolysis kettle (301) are communicated through the connecting pipe (308).
3. The automatic temperature control system for a ferric salt hydrolysis device containing metatitanic acid according to claim 1, wherein: the two outer surfaces of the first connecting block (206) are symmetrically provided with first scraping plates (208), and the outer surfaces of the first scraping plates (208) are rotationally connected with the inner surface of the first hydrolysis kettle (201).
4. The automatic temperature control system for a ferric salt hydrolysis device containing metatitanic acid according to claim 1, wherein: the inner bottom surface of the first hydrolysis kettle (201) is fixedly connected with a first bearing column (212), and the inner surface wall of the first bearing column (212) is rotationally connected with the lower end surface of the first rotating rod (205).
5. The automatic temperature control system for a ferric salt hydrolysis device containing metatitanic acid according to claim 1, wherein: the outer surfaces of the ferric salt feeding pipe (203) and the air inlet pipe (210) respectively penetrate through the upper end surface and the lower end surface of the first hydrolysis kettle (201), and the outer surfaces of the ferric salt feeding pipe (203) and the air inlet pipe (210) are respectively fixedly connected with the inner surface wall of the first hydrolysis kettle (201).
6. The automatic temperature control system for a ferric salt hydrolysis device containing metatitanic acid according to claim 2, wherein: second scrapers (306) are symmetrically arranged on the outer surfaces of two sides of the second connecting block (304), and the outer surfaces of the second scrapers (306) are rotationally connected with the inner surface of the second hydrolysis kettle (301).
7. The automatic temperature control system for a ferric salt hydrolysis device containing metatitanic acid according to claim 2, wherein: the inner bottom surface of the second hydrolysis kettle (301) is fixedly connected with a second bearing column (307), and the inner surface wall of the second bearing column (307) is rotationally connected with the lower end surface of a second rotating rod (303).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322737251.5U CN220940663U (en) | 2023-10-12 | 2023-10-12 | Automatic temperature regulating and controlling system for ferric salt hydrolysis device containing metatitanic acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322737251.5U CN220940663U (en) | 2023-10-12 | 2023-10-12 | Automatic temperature regulating and controlling system for ferric salt hydrolysis device containing metatitanic acid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220940663U true CN220940663U (en) | 2024-05-14 |
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ID=90977331
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322737251.5U Active CN220940663U (en) | 2023-10-12 | 2023-10-12 | Automatic temperature regulating and controlling system for ferric salt hydrolysis device containing metatitanic acid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220940663U (en) |
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2023
- 2023-10-12 CN CN202322737251.5U patent/CN220940663U/en active Active
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