CN220269896U - Hemisulfate centrifugal drying equipment - Google Patents
Hemisulfate centrifugal drying equipment Download PDFInfo
- Publication number
- CN220269896U CN220269896U CN202321352429.8U CN202321352429U CN220269896U CN 220269896 U CN220269896 U CN 220269896U CN 202321352429 U CN202321352429 U CN 202321352429U CN 220269896 U CN220269896 U CN 220269896U
- Authority
- CN
- China
- Prior art keywords
- centrifugal drying
- hemisulfate
- bearing table
- hot air
- tank body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000001035 drying Methods 0.000 title claims abstract description 72
- 239000002351 wastewater Substances 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 9
- 239000002699 waste material Substances 0.000 description 4
- 238000007789 sealing Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000007363 ring formation reaction Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Centrifugal Separators (AREA)
Abstract
The utility model discloses a hemisulfate centrifugal drying device, which belongs to the technical field of centrifugal drying devices, and particularly relates to a hemisulfate centrifugal drying device, which comprises a bearing table, wherein the top of the bearing table is provided with a tank body, a centrifugal drying cylinder body is arranged in the tank body, the bottom of the bearing table is provided with a driving motor, the output end of the driving motor is connected with the centrifugal drying cylinder body, one side of the tank body is provided with a drain pipe, the other side of the tank body is provided with an air outlet, the top of the tank body is provided with a tank cover, the top of the tank cover is provided with a hot air inlet, and hot air can be introduced into the centrifugal drying cylinder body through a hot air inlet arranged on the tank cover, so that the hot air can directly act on materials in the centrifugal drying cylinder body, and compared with the prior art, the drying efficiency is greatly improved by introducing the hot air from outside.
Description
Technical Field
The utility model relates to the technical field of centrifugal drying equipment, in particular to hemisulfate centrifugal drying equipment.
Background
When the hemisulfate is produced, after the synthesis reaction and the cyclization reaction, centrifugal separation and drying operation are needed, and centrifugal separation and drying equipment are needed.
The utility model discloses a centrifugal drying equipment is used in production of 3-amino-4-pyrazole formyl hemisulfate in prior art to application number CN202021683738.X, including backup pad, support barrel and sealing baffle, backup pad top middle part is through the screw connection have support barrel, the backup pad below is located support barrel is provided with the dehydration motor under, the dehydration motor with the backup pad passes through the screw connection. The beneficial effects are that: according to the centrifugal drying equipment for producing the 3-amino-4-pyrazole formyl hemisulfate, disclosed by the utility model, the output shaft of the dewatering motor is rotationally sealed through the sealing baffle and the bottom of the supporting cylinder, so that a double sealing effect can be achieved, waste water separated from the inside of the supporting cylinder is effectively prevented from leaking downwards from the output shaft of the dewatering motor, stable and safe operation of the dewatering motor can be ensured, the rotating disc is connected with the centrifugal base through the transmission pin, the centrifugal drying cylinder and the centrifugal base can be conveniently detached and installed, and then the centrifugal drying cylinder can be taken out for discharging, so that the discharging efficiency is improved.
Disclosure of Invention
This section is intended to outline some aspects of embodiments of the utility model and to briefly introduce some preferred embodiments. Some simplifications or omissions may be made in this section as well as in the description summary and in the title of the application, to avoid obscuring the purpose of this section, the description summary and the title of the utility model, which should not be used to limit the scope of the utility model.
The present utility model has been made in view of the problems existing in the conventional hemisulfate centrifugal drying apparatus.
Therefore, the utility model aims to provide the hemisulfate centrifugal drying equipment, and hot air can be introduced into the centrifugal drying cylinder through the hot air inlet arranged on the tank cover, so that the hot air can directly act on materials in the centrifugal drying cylinder, and compared with the prior art that the hot air is introduced from outside, the drying efficiency is greatly improved.
In order to solve the technical problems, according to one aspect of the present utility model, the following technical solutions are provided:
a hemisulfate centrifugal drying device comprises a bearing table;
the novel centrifugal drying tank is characterized in that the tank body is arranged at the top of the bearing table, a centrifugal drying cylinder body is arranged in the tank body, a driving motor is arranged at the bottom of the bearing table, the output end of the driving motor is connected with the centrifugal drying cylinder body, a drain pipe is arranged on one side of the tank body, an air outlet is formed in the other side of the tank body, a tank cover is arranged at the top of the tank body, and a hot air inlet is formed in the top of the tank cover.
As a preferable scheme of the hemisulfate centrifugal drying device, the utility model comprises the following steps: the bottom of the bearing table is provided with a bracket, and the bracket is positioned at four corners of the bearing table.
As a preferable scheme of the hemisulfate centrifugal drying device, the utility model comprises the following steps: the drain pipe is connected with a waste water purifying box, and a water outlet is arranged on the waste water purifying box.
As a preferable scheme of the hemisulfate centrifugal drying device, the utility model comprises the following steps: the wastewater purifying box is positioned at the top of the bearing table and is fixedly connected with the bearing table.
As a preferable scheme of the hemisulfate centrifugal drying device, the utility model comprises the following steps: and a heating ring is arranged in the inner cavity at the bottom of the centrifugal drying cylinder body.
As a preferable scheme of the hemisulfate centrifugal drying device, the utility model comprises the following steps: the tank cover is rotationally connected with the tank body, and the hot air inlet is connected with an air outlet of the air heater through a pipeline.
Compared with the prior art, the utility model has the beneficial effects that: through the hot air inlet that sets up on the cover, can let in centrifugal stoving barrel with hot-blast, therefore hot-blast can directly be on centrifugal stoving barrel internal material, compare among the prior art by outside let in hot-blast, its stoving efficiency has improved greatly.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present utility model, the following detailed description of the embodiments of the present utility model will be given with reference to the accompanying drawings, which are to be understood as merely some embodiments of the present utility model, and from which other drawings can be obtained by those skilled in the art without inventive faculty. Wherein:
FIG. 1 is a schematic diagram of the structure of the present utility model;
FIG. 2 is a schematic cross-sectional view of the present utility model;
fig. 3 is a schematic top view of the tank of the present utility model.
In the figure; 100 bearing tables, 101 supports, 110 tank bodies, 120 centrifugal drying cylinder bodies, 130 driving motors, 140 drain pipes, 150 wastewater purifying boxes, 160 water outlets, 170 air outlets, 180 tank covers and 190 hot air inlets.
Detailed Description
In order that the above objects, features and advantages of the utility model will be readily understood, a more particular description of the utility model will be rendered by reference to the appended drawings.
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 in other ways other than those described herein, and persons skilled in the art will readily appreciate that the present utility model is not limited to the specific embodiments disclosed below.
Next, the present utility model will be described in detail with reference to the drawings, wherein the sectional view of the device structure is not partially enlarged to general scale for the convenience of description, and the drawings are only examples, which should not limit the scope of the present utility model. In addition, the three-dimensional dimensions of length, width and depth should be included in actual fabrication.
For the purpose of making the objects, technical solutions and advantages of the present utility model more apparent, embodiments of the present utility model will be described in further detail below with reference to the accompanying drawings.
The utility model provides the following technical scheme: during the use process, the hot air can be introduced into the centrifugal drying cylinder through the hot air inlet arranged on the tank cover, so that the hot air can directly act on the materials in the centrifugal drying cylinder, and compared with the prior art that the hot air is introduced from outside, the drying efficiency is greatly improved;
fig. 1 to 3 are schematic structural views showing a first embodiment of a centrifugal drying apparatus for hemisulfate according to the present utility model, referring to fig. 1 to 3, a main body portion of the centrifugal drying apparatus for hemisulfate according to the present utility model includes a carrying table 100;
the top of the bearing table 100 is provided with a tank body 110, a centrifugal drying cylinder 120 is arranged in the tank body 110, the bottom of the bearing table 100 is provided with a driving motor 130, the output end of the driving motor 130 is connected with the centrifugal drying cylinder 120, one side of the tank body 110 is provided with a drain pipe 140, the other side of the tank body 110 is provided with an air outlet 170, the top of the tank body 110 is provided with a tank cover 180, the top of the tank cover 180 is provided with a hot air inlet 190, the bottom of the bearing table 100 is provided with a bracket 101, the bracket 101 is positioned at four corners of the bearing table 100, the bottom of the bearing table 100 is provided with the bracket 101, a wastewater purifying box 150 is positioned at the top of the bearing table 100 and is fixedly connected with the bearing table 100, the bottom inner cavity of the centrifugal drying cylinder 120 is provided with a heating ring, the tank cover 180 is rotationally connected with the tank body 110, the hot air inlet 190 is connected with the air outlet of a hot air blower through a pipeline, the tank body 110 is used for bearing the centrifugal drying cylinder 120, the centrifugal drying cylinder 120 is used for bearing the centrifugal treatment of the material, the centrifugal drying cylinder 120 is driven by the centrifugal drying cylinder 130, the hot air inlet 190 is used for carrying out centrifugal treatment of the material, the material is carried out through the hot air inlet conveying treatment, the centrifugal drying cylinder is used for driving the centrifugal drying cylinder 120 is used for carrying the centrifugal drying, the material, the drying cylinder is used for carrying the drying, the waste water, the drying is carried out the drying, the waste is subjected to the waste water, the waste is purified by the centrifugal drying cylinder is discharged by the centrifugal drying cylinder is used for the waste water, the waste water is discharged by the waste water, and is discharged by the centrifugal drying cylinder, and is discharged by the waste water, and is discharged by the waste air, and is used for the waste air, and is discharged by the air, and is used for the drying cylinder and is used for drying drum and is used for drying;
referring to fig. 1-3, the specific working principle of the hemisulfate centrifugal drying apparatus of the present embodiment is as follows, hot air can be introduced into the centrifugal drying cylinder 120 through the hot air inlet provided on the cover 180, so that the hot air can directly act on the material in the centrifugal drying cylinder 120, and compared with the prior art in which the hot air is introduced from the outside, the drying efficiency is greatly improved.
Although the utility model has been described hereinabove with reference to embodiments, various modifications thereof may be made and equivalents may be substituted for elements thereof without departing from the scope of the utility model. In particular, the features of the disclosed embodiments may be combined with each other in any manner as long as there is no structural conflict, and the exhaustive description of these combinations is not given in this specification merely for the sake of omitting the descriptions and saving resources. Therefore, it is intended that the utility model not be limited to the particular embodiment disclosed, but that the utility model will include all embodiments falling within the scope of the appended claims.
Claims (6)
1. A hemisulfate centrifugal drying device, which is characterized in that: comprises a bearing table (100);
the novel centrifugal drying device is characterized in that the top of the bearing table (100) is provided with a tank body (110), a centrifugal drying cylinder body (120) is arranged in the tank body (110), a driving motor (130) is arranged at the bottom of the bearing table (100), the output end of the driving motor (130) is connected with the centrifugal drying cylinder body (120), a drain pipe (140) is arranged on one side of the tank body (110), an air outlet (170) is formed in the other side of the tank body (110), a tank cover (180) is arranged at the top of the tank body (110), and a hot air inlet (190) is formed in the top of the tank cover (180).
2. The hemisulfate centrifugal drying apparatus according to claim 1, wherein: the bottom of the bearing table (100) is provided with a bracket (101), and the bracket (101) is positioned at four corners of the bearing table (100).
3. The hemisulfate centrifugal drying apparatus according to claim 1, wherein: the drain pipe (140) is connected with the waste water purifying box (150), and a drain outlet (160) is arranged on the waste water purifying box (150).
4. A hemisulfate centrifugal drying apparatus according to claim 3, wherein: the wastewater purifying box (150) is positioned at the top of the bearing table (100) and is fixedly connected with the bearing table (100).
5. The hemisulfate centrifugal drying apparatus according to claim 1, wherein: and a heating ring is arranged in the inner cavity at the bottom of the centrifugal drying cylinder body (120).
6. The hemisulfate centrifugal drying apparatus according to claim 1, wherein: the tank cover (180) is rotationally connected with the tank body (110), and the hot air inlet (190) is connected with an air outlet of the air heater through a pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321352429.8U CN220269896U (en) | 2023-05-31 | 2023-05-31 | Hemisulfate centrifugal drying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321352429.8U CN220269896U (en) | 2023-05-31 | 2023-05-31 | Hemisulfate centrifugal drying equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220269896U true CN220269896U (en) | 2023-12-29 |
Family
ID=89297858
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321352429.8U Active CN220269896U (en) | 2023-05-31 | 2023-05-31 | Hemisulfate centrifugal drying equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220269896U (en) |
-
2023
- 2023-05-31 CN CN202321352429.8U patent/CN220269896U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205980584U (en) | Medicinal material compounding device that has stoving function convenient to ejection of compact | |
| CN205856291U (en) | A kind of high-efficiency environment friendly mud drying forming equipment | |
| CN104150726B (en) | A kind of sludge treatment equipment of minimizing and sludge drying method | |
| CN106430809A (en) | Sewage and sludge treatment system and environmental-friendly recycling method thereof | |
| CN1990505A (en) | Methods for preparing alkali cellulose and cellulose ether | |
| CN111018293A (en) | Device for preparing composite biochar by co-pyrolysis of sludge and biomass and use method thereof | |
| CN220269896U (en) | Hemisulfate centrifugal drying equipment | |
| CN215236151U (en) | Asparagus medicinal material washs stoving integration equipment | |
| CN107365041A (en) | A kind of circulating sludge treatment equipment | |
| CN206337132U (en) | A kind of roller fermentation tank | |
| CN207537320U (en) | A kind of efficient municipal sludge drying breaking means | |
| CN204824568U (en) | Mud decrement processing system | |
| CN206534036U (en) | A kind of tealeaves cake of press device | |
| CN212917518U (en) | Production device for preparing precoated sand by environment-friendly hot-method precoating | |
| CN211695621U (en) | A rapid drainer for rice bran crude oil refining purification | |
| CN204902472U (en) | Cylinder drying -machine of water purification filter material | |
| CN104772090B (en) | Apparatus for manufacturing clean fuel through papermaking waste | |
| CN206279072U (en) | A kind of biological dewatered device of roller | |
| CN209502533U (en) | A kind of garbage aerobic fermentation device | |
| CN206986591U (en) | A kind of continuous type discards paper pulper | |
| CN207471970U (en) | A kind of solid refuse drying unit | |
| CN206428134U (en) | A kind of roller fermentation tank for heat pump auxiliary sludge organism anhydration system | |
| CN214693811U (en) | Sludge dewatering equipment for sewage treatment station | |
| CN206069679U (en) | A kind of sludge thin layer desiccation apparatus | |
| CN206051551U (en) | Chilling roll |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |