CN209464615U - It is a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin - Google Patents
It is a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin Download PDFInfo
- Publication number
- CN209464615U CN209464615U CN201920119967.XU CN201920119967U CN209464615U CN 209464615 U CN209464615 U CN 209464615U CN 201920119967 U CN201920119967 U CN 201920119967U CN 209464615 U CN209464615 U CN 209464615U
- Authority
- CN
- China
- Prior art keywords
- formaldehyde resin
- phenol formaldehyde
- producing
- drying
- sulfonated phenol
- 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.)
- Expired - Fee Related
Links
- 238000001035 drying Methods 0.000 title claims abstract description 46
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical class [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 241000405070 Percophidae Species 0.000 claims abstract description 15
- 238000009690 centrifugal atomisation Methods 0.000 claims abstract description 15
- 230000000007 visual effect Effects 0.000 claims abstract description 12
- 239000011521 glass Substances 0.000 claims description 2
- 241000272525 Anas platyrhynchos Species 0.000 claims 1
- 238000000703 high-speed centrifugation Methods 0.000 claims 1
- 239000003595 mist Substances 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 7
- 239000003292 glue Substances 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000007599 discharging Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000000889 atomisation Methods 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- -1 feeding pump 1 Chemical class 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 238000006277 sulfonation reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin, it is characterized by comprising feeding pump (1), air heater (2), hot-air distributor (3), high speed centrifugal atomization device (4) and drying towers (5), the centrifugal atomizing disk (6) of the high speed centrifugal atomization device (4) is equipped with Duckbill type nozzle (9), airlock (8) are equipped between the drying tower (5) and discharge port (12), are equipped with visual windows (7) in the middle part of the drying tower (5).The utility model provide a kind of atomizing effect it is excellent, it is high-efficient, reduce material and glue wall, while convenient for observation and the drying equipment for steady, the high-efficient production sulfonated phenol formaldehyde resin that discharges.
Description
Technical field
The utility model relates to sulfonated phenol formaldehyde resin production technical fields, especially a kind of for producing sulfonated phenol formaldehyde resin
Drying equipment.
Background technique
The drying equipment for producing sulfonation sulfonated phenol formaldehyde resin on the market at present mostly uses greatly spray drying, and principle is in dry
By the material and hot air after atomization in dry tower, moisture rapid vaporization obtains dry products, the method for changing can directly make solution,
Dry emulsion is in powdered or particulate preparation, can save the processes such as devaporation, crushing.
Currently, in the prior art, the thing liquid that the centrifugal atomizing disk nozzle of centrifugal atomizer sprays is thicker, and atomizing effect is poor,
Low efficiency, when feeding speed increases, fluid column is easy to be directly sprayed on dry inner wall of tower, limits feeding speed and be easy to cause
Thing liquid glues wall waste.The problems such as existing drying equipment is there is also inconvenient observation simultaneously, and discharge low efficiency, and effect is poor, therefore mention
, reduction material excellent, high-efficient for a kind of atomizing effect glues wall, while convenient for observation and steady, the high-efficient production that discharges
The drying equipment of sulfonated phenol formaldehyde resin, becomes urgent problem to be solved.
Utility model content
The shortcomings that the purpose of the utility model is to overcome the prior arts, provide a kind of atomizing effect it is excellent, it is high-efficient, subtract
Few material glues wall, while convenient for observation and the drying equipment for the production sulfonated phenol formaldehyde resin for discharging steady, high-efficient.
The purpose of this utility model is achieved through the following technical solutions:
It is a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin, it is characterised in that: including feeding pump, air heater,
One end of hot-air distributor, high speed centrifugal atomization device and drying tower, air heater is connect with air inlet, the other end and hot wind point
Orchestration connection, hot-air distributor are set to the top of drying tower, and drying tower is hollow structure and its bottom is provided with discharge port,
High speed centrifugal atomization device is connect with hot-air distributor, and one end of feeding pump is connect with high speed centrifugal atomization device, the other end and charging
The centrifugal atomizing disk of mouth connection, the high speed centrifugal atomization device is equipped with Duckbill type nozzle, sets between the drying tower and discharge port
There is airlock, is equipped with visual windows in the middle part of the drying tower.
The Duckbill type nozzle includes connector and Duckbill type outlet.
The connector is cylinder, and upper end is equipped with screw thread.
The drying tower upper end is cylinder, and lower end is taper.
The visual windows are equipped with visual glass.
The utility model has the advantage that
1, Duckbill type nozzle is set, improves atomizing effect, improves efficiency, greatly reduces thing liquid and glues showing for wall
As achieving the purpose that material makes full use of, and can improve efficiency by way of improving feeding speed.
2, visual windows are set, observation is facilitated.
3, airlock is set, so that discharging is steady, improves discharging efficiency.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the main view of Duckbill type nozzle；
Fig. 3 is the A-A cross-sectional view of Fig. 2；
In figure: 1- feeding pump, 2- air heater, 3- hot-air distributor, 4- high speed centrifugal atomization device, 5- drying tower, 6-
Centrifugal atomizing disk, 7- visual windows, 8- airlock, 9- Duckbill type nozzle, the outlet of 10- Duckbill type, 11- connector, 12- discharging
Mouthful, 13- feed inlet, 14- air inlet.
Specific embodiment
The utility model is further described with reference to the accompanying drawing, but the protection scope of the utility model be not limited to
It is lower described.
As shown in Figure 1, a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin, including feeding pump 1, air heater 2,
One end of hot-air distributor 3, high speed centrifugal atomization device 4 and drying tower 5, air heater 2 is connect with air inlet 14, the other end with
Hot-air distributor 3 connects, and hot-air distributor 3 is set to the top of drying tower 5, and drying tower 5 is hollow structure and sets in its bottom
It is equipped with discharge port 12, high speed centrifugal atomization device 4 is connect with hot-air distributor 3, one end of feeding pump 1 and high speed centrifugal atomization device 4
Connection, the other end are connect with feed inlet 13, and the centrifugal atomizing disk 6 of the high speed centrifugal atomization device 4 is equipped with Duckbill type nozzle 9, institute
It states and is equipped with airlock (8) between drying tower 5 and discharge port 12, visual windows 7 are equipped in the middle part of the drying tower 5.
As shown in Fig. 2, Fig. 3, the Duckbill type nozzle 9 include connector 11 and Duckbill type outlet 10, the connection, 11
For cylinder, and upper end is equipped with screw thread, is connected through a screw thread, Duckbill type is provided in replacement easy to disassemble, jet expansion, improves
Atomizing effect improves efficiency, greatly reduces the phenomenon that thing liquid glues wall, achievees the purpose that material makes full use of, and can
It is improved efficiency in a manner of by improving feeding speed.
Preferably, 5 upper end of drying tower be cylinder, lower end is taper, and cylindrical structure has greater room, facilitate material with
Hot-air comes into full contact with, and drying tower 5 is smoothly discharged in the material that conical structure is conducive to after drying.
By the visual windows 7 of setting, facilitate observation, while drying tower can be cleared up by visual windows, it is a degree of
Facilitate cleaning.
Discharging efficiency is improved so that discharging is steady by the airlock 8 of setting.
The course of work of the utility model is as follows: in use, open feeding pump 1 and air heater 2, hot wind is from air inlet
14 enter air heater 2, and the hot-air distributor 3 at 5 top of drying tower is entered after heating, and hot-air distributor 3 is uniform by hot-air
Ground enters in drying tower 5, and rotation is downwardly into 5 bottom of drying tower in the shape of a spiral；Material by feed inlet 13 through feeding pump 1 into
Enter the high speed centrifugal atomization device 4 at 5 top of drying tower, is sprayed after material atomization by the Duckbill type nozzle 9 of centrifugal atomizing disk 6, and
With the hot air entered in drying tower 5, rapid vaporization is dried to powder-product, and dry powder-product passes through airlock 8
Steady discharging collects finished product by discharge port 12, and can be seen drying process by visual windows 7 in the process, in order to carry out pair
The adjusting of charging rate.
Claims (5)
1. a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin, it is characterised in that: including feeding pump (1), air heater
(2), hot-air distributor (3), high speed centrifugal atomization device (4) and drying tower (5), one end of air heater (2) and air inlet
(14) it connects, the other end is connect with hot-air distributor (3), and hot-air distributor (3) is set to the top of drying tower (5), drying tower
(5) it is hollow structure and is provided with discharge port (12) in its bottom, high speed centrifugal atomization device (4) is connect with hot-air distributor (3),
One end of feeding pump (1) is connect with high speed centrifugal atomization device (4), and the other end is connect with feed inlet (13), the high speed centrifugation mist
The centrifugal atomizing disk (6) for changing device (4) is equipped with Duckbill type nozzle (9), is equipped between the drying tower (5) and discharge port (12) and closes wind
Device (8), drying tower (5) middle part are equipped with visual windows (7).
2. according to claim 1 a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin, it is characterised in that: the duck
Nozzle type nozzle (9) includes connector (11) and Duckbill type outlet (10).
3. according to claim 2 a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin, it is characterised in that: the company
Junctor (11) is cylinder, and upper end is equipped with screw thread.
4. according to claim 1 a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin, it is characterised in that: described dry
Dry tower (5) upper end is cylinder, and lower end is taper.
5. according to claim 1 a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin, it is characterised in that: it is described can
Viewing window (7) is equipped with visual glass.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920119967.XU CN209464615U (en) | 2019-01-24 | 2019-01-24 | It is a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920119967.XU CN209464615U (en) | 2019-01-24 | 2019-01-24 | It is a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209464615U true CN209464615U (en) | 2019-10-08 |
Family
ID=68091370
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920119967.XU Expired - Fee Related CN209464615U (en) | 2019-01-24 | 2019-01-24 | It is a kind of for producing the drying equipment of sulfonated phenol formaldehyde resin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209464615U (en) |
-
2019
- 2019-01-24 CN CN201920119967.XU patent/CN209464615U/en not_active Expired - Fee Related
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Legal Events
| 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: 20191008 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |