CN211987137U - Spray drying tower for pulverizing - Google Patents
Spray drying tower for pulverizing Download PDFInfo
- Publication number
- CN211987137U CN211987137U CN202020594727.8U CN202020594727U CN211987137U CN 211987137 U CN211987137 U CN 211987137U CN 202020594727 U CN202020594727 U CN 202020594727U CN 211987137 U CN211987137 U CN 211987137U
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- Prior art keywords
- fixedly connected
- pipe
- tower body
- base
- box
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- 238000001694 spray drying Methods 0.000 title claims abstract description 19
- 238000010298 pulverizing process Methods 0.000 title claims description 11
- 239000007788 liquid Substances 0.000 claims abstract description 42
- 238000001816 cooling Methods 0.000 claims abstract description 39
- 238000010438 heat treatment Methods 0.000 claims abstract description 38
- 238000000034 method Methods 0.000 claims abstract description 14
- 230000008569 process Effects 0.000 claims abstract description 10
- 239000000843 powder Substances 0.000 claims abstract description 8
- 238000007599 discharging Methods 0.000 claims abstract description 3
- 238000001035 drying Methods 0.000 abstract description 22
- 239000002699 waste material Substances 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 10
- 239000000110 cooling liquid Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a drying tower technical field just discloses a spray drying tower for powder process, which comprises a base, the top fixedly connected with pillar of base, the top fixedly connected with tower body of pillar, the outer wall fixedly connected with cooling tube of tower body, the top fixedly connected with discharging pipe of tower body, the top fixedly connected with accuse pressure valve of tower body, the top fixedly connected with cooler bin of base, the top fixedly connected with liquid pump of cooler bin, the top fixedly connected with heating cabinet of base, the inside fixedly connected with heater strip of heating cabinet, the left side fixedly connected with air duct of air pump, the top fixedly connected with control box of base. This spray drying tower for powder process possesses the convenience and cools down to the drying tower body, improves the efficiency and the quality of processing, and the temperature of convenient reuse tower body reduces the waste of energy and the inside atmospheric pressure of convenient control drying tower advantage such as.
Description
Technical Field
The utility model relates to a drying tower technical field specifically is a spray drying tower for powder process.
Background
Spray drying is a drying process in which a raw material liquid is put into an atomizer to be separated into fog drops, and a method of directly contacting the fog drops with hot air or other gases is used for obtaining a product in a particle shape.
Present drying tower wide application, however drying tower itself still has some not enoughly, and when drying tower dried, the temperature of tower body can too rise, influences the efficiency and the quality of processing, and the inconvenient reuse of drying tower's temperature, produces thermal waste, and the inside atmospheric pressure of drying tower is difficult to control, so has proposed a spray drying tower for the powder process and has solved above-mentioned problem.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
The utility model provides a not enough to prior art, the utility model provides a spray drying tower for powder process possesses the convenience and cools down to the drying tower body, the efficiency and the quality of processing are improved, the temperature of convenient reuse tower body reduces advantages such as the waste of energy and the inside atmospheric pressure of convenient control drying tower, when having solved the drying tower and having carried out the drying, the temperature of tower body can excessively rise, influence the efficiency and the quality of processing, and the inconvenient reuse of temperature of drying tower, produce thermal waste, and the inside atmospheric pressure of drying tower is difficult to the problem of control.
(II) technical scheme
For realizing above-mentioned convenience and cooling down the drying tower body, improve the efficiency and the quality of processing, the waste of the temperature reduction energy of convenient reuse tower body and the purpose of the inside atmospheric pressure of convenient control drying tower, the utility model provides a following technical scheme: a spray drying tower for pulverizing comprises a base, wherein a pillar is fixedly connected to the top of the base, a tower body is fixedly connected to the top of the pillar, a cooling pipe is fixedly connected to the outer wall of the tower body, a discharging pipe is fixedly connected to the top of the tower body, a pressure control valve is fixedly connected to the top of the tower body, a cooling box is fixedly connected to the top of the base, a liquid pump is fixedly connected to the top of the cooling box, a liquid pipe is fixedly connected to the top of the liquid pump, a heating pipe is fixedly connected to one end, away from the liquid pipe, of the cooling pipe, an air box is fixedly connected to the top of the base, an air inlet pipe is fixedly connected to the top of the air box, a heating box is fixedly connected to the top of the base, a heating wire is fixedly connected to the inside of, the top of base fixedly connected with control box.
Preferably, the number of the support columns is at least three, the bottom of the tower body is hemispherical, the cooling pipe is a spiral cooling pipe, and the top of the air guide pipe is fixedly connected with the tower body.
Preferably, the bottom fixedly connected with inlet pipe of tower body, the pressure control valve is electronic pressure control valve, and the outer wall fixedly connected with barometer that the pressure control valve was pressed, the bottom fixedly connected with bevel net that the pressure control valve was pressed.
Preferably, the cooling box and the liquid pump are fixedly connected through a guide pipe, the liquid pipe is an L-shaped liquid pipe, the right side of the liquid pipe is fixedly connected with the cooling pipe, and the air box and the heating box are fixedly connected through a guide pipe.
Preferably, the outer wall of the air box is fixedly connected with a heating pipe, one end of the heating pipe, far away from the cooling pipe, is fixedly connected with the back of the cooling box, the air pump is a centrifugal air pump, and the air pump and the heating box are fixedly connected through a guide pipe.
Preferably, the controller of the liquid pump, the controller of the control pressure valve, the controller of the heating wire and the controller of the air pump are electrically connected with the inside of the control box.
(III) advantageous effects
Compared with the prior art, the utility model provides a spray drying tower for powder process possesses following beneficial effect:
the spray drying tower for pulverizing comprises a liquid pump on a control box, a liquid pipe, a cooling pipe, a heating box, a gas tank, a control box, a gas pump, a barometer, a pressure control valve, a liquid pump, a liquid storage tank, a liquid outlet pipe and a liquid outlet pipe, wherein the liquid inlet pipe is connected with the liquid storage tank and the liquid outlet pipe, the liquid outlet pipe is connected with the liquid storage tank, the liquid outlet pipe is connected with, the drying tower body is conveniently cooled, the processing efficiency and quality are improved, the temperature of the tower body is conveniently recycled, the energy is reduced, the air pressure inside the drying tower is conveniently controlled, and therefore the use of a user is facilitated.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
In the figure: the device comprises a base 1, a support 2, a tower body 3, a cooling pipe 4, a discharge pipe 5, a pressure control valve 6, a cooling tank 7, a liquid pump 8, a liquid pipe 9, a heating pipe 10, an air tank 11, an air inlet pipe 12, a heating tank 13, a heating wire 14, an air pump 15, an air guide pipe 16 and a control box 17.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1, a spray drying tower for pulverizing powder comprises a base 1, a top of the base 1 is fixedly connected with pillars 2, the number of the pillars 2 is at least three, the bottom of the tower 3 is hemispherical, cooling pipes 4 are spiral cooling pipes, the top of an air duct 16 is fixedly connected with the tower 3, the top of the pillars 2 is fixedly connected with the tower 3, the bottom of the tower 3 is fixedly connected with a feed pipe, a pressure control valve 6 is an electric pressure control valve, the outer wall of the pressure control valve 6 is fixedly connected with a barometer, the bottom of the pressure control valve 6 is fixedly connected with a bevel net, the outer wall of the tower 3 is fixedly connected with the cooling pipes 4, the top of the tower 3 is fixedly connected with a discharge pipe 5, the top of the tower 3 is fixedly connected with the pressure control valve 6, the top of the base 1 is fixedly connected with a cooling box 7, the cooling box 7 and a liquid pump 8 are fixedly connected by a conduit, the air box 11 and the heating box 13 are fixedly connected by a guide pipe, the top fixedly connected with liquid pump 8 of the cooling box 7, the top fixedly connected with liquid pipe 9 of the liquid pump 8, one end fixedly connected with heating pipe 10 of the liquid pipe 9 is kept away from the cooling pipe 4, the top fixedly connected with air box 11 of the base 1, the outer wall fixedly connected with heating pipe 10 of the air box 11, the back of the one end fixedly connected with cooling box 7 of the cooling pipe 4 is kept away from the heating pipe 10, the air pump 15 is a centrifugal air pump, the air pump 15 and the heating box 13 are fixedly connected by a guide pipe, the top fixedly connected with air inlet pipe 12 of the air box 11, the top fixedly connected with heating box 13 of the base 1, the internal fixedly connected with heating wire 14 of the heating box 13, the top fixedly connected with air pump 15 of the base 1, the left side fixedly connected with air guide pipe 16 of the air pump 15, the, A controller for the pressure control valve 6, a controller for the heating wire 14 and a controller for the air pump 15.
To sum up, in the spray drying tower for pulverizing, the liquid pump 8 on the control box 17 is controlled by the control box 17 to pump the cooling liquid in the cooling box 7 to enter the liquid pipe 9, and then the cooling liquid enters the cooling pipe 4 to cool the tower body 3, then the temperature of the tower body 3 is gradually absorbed by the cooling pipe 4, so that the temperature of the cooling pipe 4 entering the heating pipe 10 rises, the gas in the gas box 11 is heated by the heating pipe 10, then the gas pump 15 is controlled by the control box 17 to pump the gas primarily heated by the heating pipe 10 in the gas box 11 to enter the heating box 13, the heating wire 14 inside the heating box 13 is controlled by the control box 17 to heat the gas again, and then the liquid in the heating pipe 10 enters the cooling box 7 for circulation after being cooled by the outer wall of the gas box 11, and then the barometer on the pressure control valve 6 is controlled by the control box 17 to detect the air pressure inside the tower body 3, and then the control accuse is pressed the closure of valve 6, is stopped the discharge that the raw materials passed through accuse pressure valve 6 by the inclined plane net of accuse pressure valve 6 bottoms, has made things convenient for and has cooled down drying tower body 3, improves the efficiency and the quality of processing, and the waste of the temperature reduction energy of convenient reuse tower body 3 and the inside atmospheric pressure of convenient control drying tower to user's use has been made things convenient for.
It is to be noted that the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising an … …" does not exclude the presence of other identical elements in a process, method, article, or apparatus that comprises the element.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The utility model provides a spray drying tower for powder process, includes base (1), its characterized in that: the tower comprises a base (1), a support column (2) and a tower body (3) fixedly connected to the top of the support column (2), a cooling pipe (4) fixedly connected to the outer wall of the tower body (3), a discharging pipe (5) fixedly connected to the top of the tower body (3), a pressure control valve (6) fixedly connected to the top of the tower body (3), a cooling box (7) fixedly connected to the top of the base (1), a liquid pump (8) fixedly connected to the top of the cooling box (7), a liquid pipe (9) fixedly connected to the top of the liquid pump (8), a heating pipe (10) fixedly connected to one end of the cooling pipe (4) far away from the liquid pipe (9), a gas tank (11) fixedly connected to the top of the base (1), an air inlet pipe (12) fixedly connected to the top of the gas tank (11), and a heating box (13) fixedly connected to the top of the base, the inside fixedly connected with heater strip (14) of heating cabinet (13), the top fixedly connected with air pump (15) of base (1), the left side fixedly connected with air duct (16) of air pump (15), the top fixedly connected with control box (17) of base (1).
2. The spray drying tower for pulverizing of claim 1, wherein: the quantity of pillar (2) is three at least, the bottom of tower body (3) is the hemisphere, cooling tube (4) are the spiral cooling tube, the top fixedly connected with tower body (3) of air duct (16).
3. The spray drying tower for pulverizing of claim 1, wherein: the bottom fixedly connected with inlet pipe of tower body (3), the accuse is pressed valve (6) and is pressed the valve for electronic accuse, and the outer wall fixedly connected with barometer that the accuse pressed valve (6), the bottom fixedly connected with bevel net that the valve (6) was pressed in the accuse.
4. The spray drying tower for pulverizing of claim 1, wherein: cooling box (7) and liquid pump (8) are by pipe fixed connection, liquid pipe (9) are L shape liquid pipe, and the right side fixedly connected with cooling tube (4) of liquid pipe (9), gas tank (11) and heating cabinet (13) are by pipe fixed connection.
5. The spray drying tower for pulverizing of claim 1, wherein: the air pump is characterized in that a heating pipe (10) is fixedly connected to the outer wall of the air box (11), the back face of the cooling box (7) is fixedly connected to one end, far away from the cooling pipe (4), of the heating pipe (10), the air pump (15) is a centrifugal air pump, and the air pump (15) and the heating box (13) are fixedly connected through a guide pipe.
6. The spray drying tower for pulverizing of claim 1, wherein: the controller of the liquid pump (8), the controller of the pressure control valve (6), the controller of the heating wire (14) and the controller of the air pump (15) are electrically connected with the inside of the control box (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020594727.8U CN211987137U (en) | 2020-04-20 | 2020-04-20 | Spray drying tower for pulverizing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020594727.8U CN211987137U (en) | 2020-04-20 | 2020-04-20 | Spray drying tower for pulverizing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211987137U true CN211987137U (en) | 2020-11-24 |
Family
ID=73416235
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020594727.8U Expired - Fee Related CN211987137U (en) | 2020-04-20 | 2020-04-20 | Spray drying tower for pulverizing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211987137U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113292590A (en) * | 2021-05-21 | 2021-08-24 | 江西国化实业有限公司 | Separation device for preparing trimethylsilyl trifluoromethanesulfonate and using method |
-
2020
- 2020-04-20 CN CN202020594727.8U patent/CN211987137U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113292590A (en) * | 2021-05-21 | 2021-08-24 | 江西国化实业有限公司 | Separation device for preparing trimethylsilyl trifluoromethanesulfonate and using method |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20201124 |
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| CF01 | Termination of patent right due to non-payment of annual fee |