CN218901756U - Granulating tower for stearate production - Google Patents
Granulating tower for stearate production Download PDFInfo
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- CN218901756U CN218901756U CN202223107486.8U CN202223107486U CN218901756U CN 218901756 U CN218901756 U CN 218901756U CN 202223107486 U CN202223107486 U CN 202223107486U CN 218901756 U CN218901756 U CN 218901756U
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Abstract
The utility model discloses a granulating tower for producing stearate, which comprises a material storage tower section, a tower body and a tower top straight pipe, wherein the top of the material storage tower section is connected with the tower body through a circular truncated cone-shaped connecting pipe B, one side of the tower body is connected with a pressure tank through a hoop, one side of the pressure tank is provided with a semiconductor refrigerator through a mounting groove, the top of the pressure tank is provided with an electric inflator pump through a screw, an output port of the pressure tank is connected with an input port of an electromagnetic valve and an output port of the electromagnetic valve is connected with an air inlet pipe, one end part of the air inlet pipe is positioned in the circular truncated cone-shaped connecting pipe B, an air outlet hole of the air inlet pipe is upwards arranged, and the inner top end of the tower top straight pipe is provided with an atomizer through a mounting frame. This novel granulation tower for stearate production can detect the air conditioning and adjust the inflow of air conditioning according to the temperature of crystallization, is fit for extensively using widely.
Description
Technical Field
The utility model relates to the technical field of prilling towers, in particular to a prilling tower for producing stearate.
Background
The tower type crystallizer is also called a granulating tower, the solution is sprayed into the tower by a sprayer, in the process of falling to the bottom of the tower, a part of solvent is vaporized in the countercurrent air flow to be cooled, so that crystals are generated, crystals and mother liquor automatically flow out or are pumped out for further refining, or the high-concentration solution is sprayed into the tower by the sprayer, cold air is fed into the lower part of the tower, in the process of falling to the bottom of the tower, the liquid drops of the solution are cooled by the cold air to be solidified into crystal particles, and the stearate crystals are prepared.
The existing granulating tower for producing the stearate has the following defects: the granulating tower for producing stearate cannot detect the temperature of the cool air and adjust the inflow amount of the cool air according to the temperature of crystallization. Therefore, we propose a prilling tower for producing stearate.
Disclosure of Invention
The utility model mainly aims to provide a granulating tower for producing stearate, which can effectively solve the problems in the background technology.
In order to achieve the above purpose, the technical scheme adopted by the utility model is as follows:
the utility model provides a prilling tower is used in stearate production, includes stock tower section, body of a tower and top of a tower straight tube, the body of a tower is connected through round platform shape connecting pipe B to the top of stock tower section, semiconductor refrigerator is installed through the mounting groove to one side of staple bolt connection overhead tank and overhead tank, electronic pump is installed through the screw at the overhead tank's top, the intake pipe is connected to the delivery outlet of the delivery outlet connection solenoid valve of overhead tank's input port and solenoid valve, the one end position of intake pipe is located round platform shape connecting pipe B and the venthole of intake pipe upwards sets up, the atomizer is installed through the mounting bracket on the interior top of a tower straight tube, install heat suction fan through the screw in overhead tank's the top welding heat delivery outlet and the heat delivery outlet.
Further, a discharge hole is formed in one side of the bottom end of the storage tower section, and a sealing cover is mounted on one side of the discharge hole through a positioning screw.
Further, a thermometer A is installed on one side of the pressure tank through a screw, and the detection end of the thermometer A is located in the pressure tank.
Further, the output end of the electric inflator pump is positioned in the pressure tank, the refrigerating end of the semiconductor refrigerator is positioned in the pressure tank, air is blown into the pressure tank through the electric inflator pump at the top of the pressure tank, and the semiconductor refrigerator is utilized to cool the air in the pressure tank.
Further, the input port of atomizer is connected with the conveyer pipe and the conveyer pipe runs through the top of the tower straight tube, and at top of the tower straight tube outside installation thermometer B is convenient for detect the temperature of atomizing into the liquid pearl and adjust the air-conditioner in the volume of letting in of certain time according to the temperature to realize the accurate of stearate crystallization.
Further, one side of the tower top straight pipe is provided with a thermometer B through a screw, and the detection end of the thermometer B is positioned in the tower top straight pipe.
Compared with the prior art, the utility model has the following beneficial effects:
1. according to the granulating tower for producing the stearate, air is blown into the pressure tank through the electric inflator pump at the top of the pressure tank, the air in the pressure tank is refrigerated and cooled by the semiconductor refrigerator, the temperature of the air in the pressure tank is detected by the thermometer A to be reduced to a specified temperature, molten stearate feed liquid is atomized Cheng Yezhu through the atomizer at the top of the tower body, low-temperature air in the pressure tank is blown out from the bottom of the granulating tower through opening the electromagnetic valve, convection is formed between the low-temperature air and atomized liquid beads, and the liquid beads at 100-180 degrees are rapidly cooled to below 40 degrees to form particles.
2. According to the granulating tower for producing the stearate, the heat generated by crystallization is rapidly discharged by the heat sucking fan arranged at the top end of the granulating tower, and the thermometer B is arranged at the outer side of the straight pipe at the tower top so as to be convenient for detecting the temperature of atomized liquid beads and adjusting the inflow of cold air for a certain time according to the temperature, so that the accurate implementation of the stearate crystallization is realized.
Drawings
Fig. 1 is a schematic diagram showing the overall structure of a prilling tower for producing stearate.
FIG. 2 is a perspective view of a prilling tower for producing stearate according to the utility model.
FIG. 3 is a side view of a prilling tower for producing stearate according to the utility model.
In the figure: 1. a set screw; 2. sealing cover; 3. a discharge port; 4. a storage tower section; 5. an air inlet pipe; 6. an electromagnetic valve; 7. a semiconductor refrigerator; 8. a thermometer A; 9. a pressure tank; 10. an electric inflator; 11. a thermometer B; 12. a delivery tube; 13. a straight pipe at the top of the tower; 14. a truncated cone-shaped connecting pipe A; 15. a tower body; 16. a truncated cone-shaped connecting pipe B; 17. an atomizer; 18. a heat sucking fan; 19. and a heat output port.
Detailed Description
The utility model is further described in connection with the following detailed description, in order to make the technical means, the creation characteristics, the achievement of the purpose and the effect of the utility model easy to understand.
As shown in fig. 1-3, a prilling tower for stearate production, including stock tower section 4, tower body 15 and top of the tower straight tube 13, the top of stock tower section 4 is through round platform shape connecting pipe B16 connection tower body 15, semiconductor refrigerator 7 is installed through the mounting groove to one side of staple bolt connection overhead tank 9 and overhead tank 9 through the staple bolt to one side of tower body 15, electric inflator 10 is installed through the screw at the top of overhead tank 9, the input port of solenoid valve 6 is connected to the delivery port of overhead tank 9 and the delivery port of solenoid valve 6 is connected intake pipe 5, one end position of intake pipe 5 is located in round platform shape connecting pipe B16 and the venthole of intake pipe 5 upwards sets up, atomizer 17 is installed through the mounting bracket in the interior top of the tower straight tube 13, heat delivery port 19 and heat suction fan 18 are installed through the screw in the overhead tank 13.
Wherein, the bottom side of stock tower section 4 is provided with discharge gate 3 and discharge gate 3 one side is installed sealed lid 2 through set screw 1.
In the embodiment, as shown in fig. 1, the positioning screw 1 is unscrewed to remove the sealing cover 2, so that the discharging is facilitated.
Wherein, thermometer A8 is installed through the screw to one side of pressure jar 9 and thermometer A8's detection end is located pressure jar 9.
In this embodiment, as shown in fig. 1, the temperature of the gas in the pressure tank 9 is detected by the thermometer A8 and reduced to a predetermined temperature.
Wherein, the output end of the electric inflator pump 10 is positioned in the pressure tank 9, and the refrigerating end of the semiconductor refrigerator 7 is positioned in the pressure tank 9.
In this embodiment, as shown in fig. 1, air is blown into the pressure tank 9 by an electric inflator 10 at the top of the pressure tank 9, and the gas in the pressure tank 9 is cooled by a semiconductor refrigerator 7.
Wherein, the input port of the atomizer 17 is connected with the conveying pipe 12, and the conveying pipe 12 penetrates through the tower top straight pipe 13.
One side of the straight pipe 13 is provided with a thermometer B11 through a screw, and the detection end of the thermometer B11 is positioned in the straight pipe 13.
In this embodiment, as shown in fig. 1, a thermometer B11 is installed outside the straight tube 13 at the top of the tower to facilitate detection of the temperature of atomized liquid beads and to adjust the amount of cold air introduced for a certain period of time according to the temperature, thereby realizing accurate crystallization of stearate.
The utility model relates to a granulating tower for producing stearate, which is characterized in that when in operation, air is blown into a pressure tank 9 through an electric air pump 10 at the top of the pressure tank 9, the air in the pressure tank 9 is refrigerated and cooled by a semiconductor refrigerator 7, the temperature of the air in the pressure tank 9 is detected by a thermometer A8 to be reduced to a specified temperature, molten stearate feed liquid is atomized Cheng Yezhu through an atomizer 17 at the top of the tower body, low-temperature air in the pressure tank 9 is blown out from the bottom of the granulating tower through opening an electromagnetic valve 6 to form convection with atomized liquid beads, the liquid beads with the temperature of 100-180 ℃ are rapidly cooled to below 40 ℃ to form particles, a heat sucking fan 18 is arranged at the top of the granulating tower to rapidly discharge heat generated by crystallization, and a thermometer B11 is arranged at the outer side of a straight pipe 13 to facilitate detection of the atomized liquid beads and adjust the inflow of cool air for a certain time according to the temperature, so that the accurate implementation of the stearate crystallization is realized.
The foregoing has shown and described the basic principles and main features of the present utility model and the advantages of the present utility model. It will be understood by those skilled in the art that the present utility model is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present utility model, and various changes and modifications may be made without departing from the spirit and scope of the utility model, which is defined in the appended claims. The scope of the utility model is defined by the appended claims and equivalents thereof.
Claims (6)
1. The utility model provides a prilling tower is used in stearate production, includes stock tower section (4), body of a tower (15) and top of a tower straight tube (13), its characterized in that: the utility model discloses a high-pressure air pump, including material storage tower section (4), tower body (15) is connected through round platform shape connecting pipe B (16) at the top of material storage tower section (4), one side of tower body (15) is through staple bolt connection overhead tank (9) and one side of overhead tank (9) is through mounting groove installation semiconductor refrigerator (7), electronic pump (10) are installed through the screw in the top of overhead tank (9), inlet pipe (5) are connected in the delivery port of solenoid valve (6) and the delivery port of solenoid valve (6) are connected to the delivery port of overhead tank (9), one end position of intake pipe (5) is in round platform shape connecting pipe B (16) and the venthole of intake pipe (5) upwards sets up, atomizer (17) are installed through the mounting bracket on the interior top of tower straight tube (13), heat extraction fan (18) are installed through the screw in top welding heat delivery port (19) and heat delivery port (19).
2. The prilling tower for producing stearate according to claim 1, wherein: a discharge hole (3) is formed in one side of the bottom end of the storage tower section (4), and a sealing cover (2) is arranged on one side of the discharge hole (3) through a positioning screw (1).
3. The prilling tower for producing stearate according to claim 1, wherein: one side of the pressure tank (9) is provided with a thermometer A (8) through a screw, and the detection end of the thermometer A (8) is positioned in the pressure tank (9).
4. The prilling tower for producing stearate according to claim 1, wherein: the output end of the electric inflator pump (10) is positioned in the pressure tank (9), and the refrigerating end of the semiconductor refrigerator (7) is positioned in the pressure tank (9).
5. The prilling tower for producing stearate according to claim 1, wherein: the input port of the atomizer (17) is connected with a conveying pipe (12), and the conveying pipe (12) penetrates through the tower top straight pipe (13).
6. The prilling tower for producing stearate according to claim 1, wherein: one side of the tower top straight pipe (13) is provided with a thermometer B (11) through a screw, and the detection end of the thermometer B (11) is positioned in the tower top straight pipe (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223107486.8U CN218901756U (en) | 2022-11-23 | 2022-11-23 | Granulating tower for stearate production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223107486.8U CN218901756U (en) | 2022-11-23 | 2022-11-23 | Granulating tower for stearate production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218901756U true CN218901756U (en) | 2023-04-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202223107486.8U Active CN218901756U (en) | 2022-11-23 | 2022-11-23 | Granulating tower for stearate production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218901756U (en) |
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2022
- 2022-11-23 CN CN202223107486.8U patent/CN218901756U/en active Active
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