CN207025261U - A kind of textile industry low boiling softener raw material prilling granulator - Google Patents
A kind of textile industry low boiling softener raw material prilling granulator Download PDFInfo
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- CN207025261U CN207025261U CN201720975988.2U CN201720975988U CN207025261U CN 207025261 U CN207025261 U CN 207025261U CN 201720975988 U CN201720975988 U CN 201720975988U CN 207025261 U CN207025261 U CN 207025261U
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- low boiling
- raw material
- reaction container
- air inlet
- textile industry
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Abstract
The utility model embodiment is related to a kind of textile industry low boiling softener raw material prilling granulator, and device includes chuck stirred tank, pressure drying machine, air inlet pipe and freezing type heat exchanger；Chuck stirred tank includes interior reaction container, jacket pipe, external jacket, agitating shaft and agitating paddle；The bottom of interior reaction container is provided with drain hole；External jacket is sleeved on the outside of the bottom of interior reaction container；The top of external jacket is provided with steam inlet；The bottom of external jacket is provided with condensation-water drain；Agitating shaft is arranged in interior reaction container；Agitating paddle is arranged on the other end of agitating shaft；Charging aperture is provided with the top of pressure drying machine；Jacket pipe is connected with charging aperture and drain hole respectively；The side wall of pressure drying machine offers cold air air inlet, and cold air air inlet is connected with one end of air inlet pipe；The venthole of freezing type heat exchanger is connected with the other end of air inlet pipe.The utility model avoids contamination of products, improves product quality and production efficiency, meets the requirement of rear end different clients dispersiveness.
Description
Technical field
It the utility model is related to Chemical Manufacture equipment technology field, more particularly to a kind of textile industry low boiling softener original
Expect prilling granulator.
Background technology
At present, the softener front end raw material in textile industry is carried out broken generally by slice process, then again by
Softener is processed into back-end client's manufacture.But impurity is readily incorporated in slicing processes, granulation uniformity is poor, adds
The work load of staff, operating efficiency is low, and batch production production capacity is low, and the rear end part client that cuts into slices needs scattered make
With the jitter time used in it is grown, and dispersion effect is poor.
Therefore, in order to avoid contamination of products, improve particle uniformly, meet that different clients dispersiveness in rear end requires, in the market
It is badly in need of a kind of low boiling softener raw material prilling granulator that can solve the problem that above mentioned problem.
Utility model content
The purpose of this utility model is the problem of presence for prior art, there is provided one kind avoids contamination of products, raising
Grain is uniform, meets the textile industry low boiling softener raw material prilling granulator that rear end different clients dispersiveness requires.
To achieve the above object, the utility model provides a kind of textile industry low boiling softener raw material prilling granulator,
Device includes chuck stirred tank, pressure drying machine, air inlet pipe and freezing type heat exchanger；
The chuck stirred tank includes interior reaction container, jacket pipe, external jacket, agitating shaft and agitating paddle；
Charge door is provided with the top of the interior reaction container；The bottom of the interior reaction container is provided with drain hole, the drain hole
It is connected with one end of the jacket pipe；Frame is also arranged at the top of the interior reaction container；The frame is provided with motor；
The external jacket, the outside of the bottom of the interior reaction container being sleeved on, the bottom of the external jacket has preformed hole,
The drain hole in the preformed hole by stretching out outside the external jacket；The top of the external jacket is provided with steam inlet；Institute
The bottom for stating external jacket is provided with condensation-water drain；
The agitating shaft, in the interior reaction container；One end of the agitating shaft and the drive end phase of the motor
Even；
The agitating paddle, installed in the other end of the agitating shaft；
Charging aperture is provided with the top of the pressure drying machine, the charging aperture is connected with the other end of the jacket pipe；Institute
The side wall for stating pressure drying machine offers cold air air inlet, and the cold air air inlet is connected with one end of the air inlet pipe；
The bottom of the pressure drying machine is provided with discharging opening；
The venthole of the freezing type heat exchanger is connected with the other end of the air inlet pipe.
Preferably, impingement baffle, the position phase of the position of the impingement baffle and the steam inlet are provided with the external jacket
It is corresponding.
Preferably, the jacket pipe is provided with suction pump.
Preferably, the outer surface lower end fixed cover of the pressure drying machine is equipped with bearing.
Preferably, the jacket pipe is the body being made up of the inside of 304 stainless steels and the jackets outer wall of carbon steel.
Preferably, the inside pipe of the freezing type heat exchanger is 304 stainless pipes, the freezing type heat exchanger
Jackets outer wall be carbon steel outer wall.
Preferably, the agitating paddle is equidistantly mounted on the other end of the agitating shaft.
The textile industry low boiling softener raw material prilling granulator that the utility model embodiment provides, using pressure drying machine
It is combined with freezing type heat exchanger so that the low boiling softener liquid dissolved by heating is inside pressure drying machine with passing through
The cold air contact that freezing heat-exchanger conveying comes, air curing is granulated low boiling softener liquid to the cold, whole granulation process
Carried out in confined space, avoid pollution of the introduced contaminants to product, improve product quality, meanwhile, the size energy of particle
Enough it is adjusted by atomizer, and the uniformity of particle can be ensured, so as to meets the scattered need of rear end different clients
Ask, shorten the jitter time in back-end client's production process, reduce cost.
Brief description of the drawings
Fig. 1 is the structural representation for the textile industry low boiling softener raw material prilling granulator that the utility model embodiment provides
Figure；
Fig. 2 is the textile industry low boiling softener raw material prilling granulator chuck stirred tank that the utility model embodiment provides
Structural representation；
Fig. 3 is the partial enlargement for the textile industry low boiling softener raw material prilling granulator that the utility model embodiment provides
Figure.
Embodiment
Below by drawings and examples, the technical solution of the utility model is described in further detail.
The utility model embodiment is related to the textile industry low boiling softener raw material prilling granulator of offer, batch production production
It can greatly improve, the granular size after granulation can be adjusted by the atomizer in pressure drying machine, in closed space
Carry out, avoid material in slicing processes and be contaminated, meet the scattered requirement of rear end different clients, shorten client and produced
Jitter time in journey, reduces cost.
Fig. 1 is the structural representation for the textile industry low boiling softener raw material prilling granulator that the utility model embodiment provides
Figure.With reference to shown in Fig. 1：
Chuck stirred tank 1 and freezing type heat exchanger 3 are connected with pressure drying machine 2；Chuck stirred tank 1 and pressure drying
It is connected with each other between machine 2 by jacket pipe 10, jacket pipe 10 is preferably by the inside of 304 stainless steels and the jackets outer wall group of carbon steel
Into body, meanwhile, jacket pipe 10 is provided with suction pump 22；Pass through air inlet between freezing type heat exchanger 3 and pressure drying machine 2
Pipe 18 is connected with each other.
The top of pressure drying machine 2 is provided with charging aperture 15, and charging aperture 15 is connected with the other end of jacket pipe 10；Pressure drying
The side wall of machine 2 offers cold air air inlet 17, and cold air air inlet 17 is connected with one end of air inlet pipe 18；Pressure drying machine 2
Bottom be provided with discharging opening 16；The outer surface lower end fixed cover of pressure drying machine 2 is equipped with bearing 20, and bearing 20 is used for pressure
Drying machine 2 is fixedly mounted on required position.
The venthole of freezing type heat exchanger 3 is connected with the other end of air inlet pipe 18；The inner circular of freezing type heat exchanger 3
Pipe is preferably 304 stainless pipes, and the jackets outer wall of freezing type heat exchanger 3 is preferably carbon steel outer wall.
As shown in Figure 1, the overall knot of the utility model embodiment textile industry low boiling softener raw material prilling granulator
Annexation between structure and its each several part.With reference to Fig. 2 and Fig. 3, the concrete structure of chuck stirred tank is introduced.
Fig. 2, Fig. 3 are respectively the textile industry low boiling softener raw material prilling granulator folder that the utility model embodiment provides
Cover the structural representation and partial enlarged drawing of stirred tank.With reference to shown in Fig. 2, Fig. 3：
Chuck stirred tank 1 includes interior reaction container 4, jacket pipe 10, external jacket 5, agitating shaft 6 and agitating paddle 7.
The top of interior reaction container 4 is provided with charge door 8；The bottom of interior reaction container 4 is provided with drain hole 9, drain hole 9 and jacket pipe
10 one end is connected；The top of interior reaction container 4 is also arranged frame 11；Frame 11 is provided with motor 12.
External jacket 5, is sleeved on the outside of the bottom of interior reaction container 4, and the bottom of external jacket 5 has preformed hole 21, drain hole 9
By being stretched out in preformed hole 21 outside external jacket 5；The top of external jacket 5 is provided with steam inlet 13；The bottom of external jacket 5 is provided with cold
Condensate outlet 14；Impingement baffle 19 is provided with external jacket 5, the position of impingement baffle 19 is corresponding with the position of steam inlet 13, erosion control
Plate 19 avoids chuck stirred tank 1 and damaged due to washing away for a long time, improves the service life of chuck stirred tank 1.
Agitating shaft 6, in interior reaction container 4；One end of agitating shaft 6 is connected with the drive end of motor 12.
Agitating paddle 7, installed in the other end of agitating shaft 6.
Above is to the present embodiment provide textile industry low boiling softener raw material prilling granulator all parts, they
Between annexation and complete structure be described, it is former to textile industry low boiling softener with reference to Fig. 1-Fig. 3
The operation principle of material prilling granulator is described in detail.
In the present embodiment, the low boiling softener raw material of textile industry is put into chuck at charge door 8 first to stir
In the interior reaction container 4 for mixing kettle 1, then vapours is poured into external jacket 5 at steam inlet 13, it is low in internal reaction container 4
Boiling point softener raw material is heated so that it is low boiling softener liquid that low boiling softener raw material, which dissolves by heating, vapours
The globule is condensed into, and is flowed out from condensation-water drain 14, meanwhile, start the motor 12 in frame 11, the drive end of motor 12 drives
Agitating shaft 6 and multigroup agitating paddle 7 thereon are rotated, and low boiling softener raw material is stirred, and accelerate low boiling softener former
The conversion of material.Flowed into jacket pipe 10, and be pumped into by suction pump 22 in pressure drying machine 2, jacket pipe 10 by drain hole 9 afterwards
For the body being made up of the inside of 304 stainless steels and the jackets outer wall of carbon steel, there is insulation, pass through 2-20MPa height
Press in atomizer that low boiling softener liquid is sent in pressure drying machine 2 and be atomized into drop, so as to increase and cold air
The area of contact.
Cold air is transported in pressure drying machine 2 by freezing type heat exchanger 3 by air inlet pipe 18, low boiling softener liquid
Air curing is granulated body to the cold, and its granular size can be adjusted according to atomizer, meet the scattered need of rear end different clients
Ask, be granulated after completing, particle taken out at discharging opening 16, so as to complete whole granulation process.
The textile industry low boiling softener raw material prilling granulator that the utility model embodiment provides, chuck stirred tank 1, folder
Sleeve pipe 10 can select the one way in which of steam, conduction oil, heating water bath etc. to be heated according to different material；Pressure
Drying machine 2 can select the pressure atomization disk of different size according to different material, and adverse current, cocurrent, inverse can be selected in drying machine main body
The one of which of the different subjects such as stream+cocurrent construction；Freezing type heat exchanger 3 can as needed from chilled brine heat exchange or
The one of which of person's low-temperature cold water heat exchanger.
The textile industry low boiling softener raw material prilling granulator that the utility model embodiment provides, using pressure drying machine
It is combined with freezing type heat exchanger so that the low boiling softener liquid dissolved by heating is inside pressure drying machine with passing through
The cold air contact that freezing heat-exchanger conveying comes, air curing is granulated low boiling softener liquid to the cold, whole granulation process
Carried out in confined space, avoid pollution of the introduced contaminants to product, improve product quality, meanwhile, the size energy of particle
Enough it is adjusted by atomizer, and the uniformity of particle can be ensured, so as to meets the scattered need of rear end different clients
Ask, shorten the jitter time in back-end client's production process, reduce cost.
Above-described embodiment, the purpose of this utility model, technical scheme and beneficial effect are entered
One step describes in detail, should be understood that and the foregoing is only specific embodiment of the present utility model, is not used to limit
Determine the scope of protection of the utility model, it is all within the spirit and principles of the utility model, any modification for being made, equally replace
Change, improve, should be included within the scope of protection of the utility model.
Claims (7)
1. a kind of textile industry low boiling softener raw material prilling granulator, it is characterised in that described device includes：Chuck stirs
Kettle, pressure drying machine, air inlet pipe and freezing type heat exchanger；
The chuck stirred tank includes interior reaction container, jacket pipe, external jacket, agitating shaft and agitating paddle；
Charge door is provided with the top of the interior reaction container；The bottom of the interior reaction container is provided with drain hole, the drain hole and institute
The one end for stating jacket pipe is connected；Frame is also arranged at the top of the interior reaction container；The frame is provided with motor；
The external jacket, the outside of the bottom of the interior reaction container is sleeved on, the bottom of the external jacket has preformed hole, described
Drain hole in the preformed hole by stretching out outside the external jacket；The top of the external jacket is provided with steam inlet；It is described outer
The bottom of chuck is provided with condensation-water drain；
The agitating shaft, in the interior reaction container；One end of the agitating shaft is connected with the drive end of the motor；
The agitating paddle, installed in the other end of the agitating shaft；
Charging aperture is provided with the top of the pressure drying machine, the charging aperture is connected with the other end of the jacket pipe；The pressure
The side wall of power drying machine offers cold air air inlet, and the cold air air inlet is connected with one end of the air inlet pipe；It is described
The bottom of pressure drying machine is provided with discharging opening；
The venthole of the freezing type heat exchanger is connected with the other end of the air inlet pipe.
2. textile industry low boiling softener raw material prilling granulator according to claim 1, it is characterised in that the outer clip
Impingement baffle is provided with set, the position of the impingement baffle is corresponding with the position of the steam inlet.
3. textile industry low boiling softener raw material prilling granulator according to claim 1, it is characterised in that the chuck
Pipe is provided with suction pump.
4. textile industry low boiling softener raw material prilling granulator according to claim 1, it is characterised in that the pressure
The outer surface lower end fixed cover of drying machine is equipped with bearing.
5. textile industry low boiling softener raw material prilling granulator according to claim 1, it is characterised in that the chuck
Manage the body to be made up of the inside of 304 stainless steels and the jackets outer wall of carbon steel.
6. textile industry low boiling softener raw material prilling granulator according to claim 1, it is characterised in that the freezing
The inside pipe of formula heat exchanger is 304 stainless pipes, and the jackets outer wall of the freezing type heat exchanger is carbon steel outer wall.
7. textile industry low boiling softener raw material prilling granulator according to claim 1, it is characterised in that the stirring
Oar is equidistantly mounted on the other end of the agitating shaft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720975988.2U CN207025261U (en) | 2017-08-07 | 2017-08-07 | A kind of textile industry low boiling softener raw material prilling granulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720975988.2U CN207025261U (en) | 2017-08-07 | 2017-08-07 | A kind of textile industry low boiling softener raw material prilling granulator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207025261U true CN207025261U (en) | 2018-02-23 |
Family
ID=61474354
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720975988.2U Active CN207025261U (en) | 2017-08-07 | 2017-08-07 | A kind of textile industry low boiling softener raw material prilling granulator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207025261U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113332925A (en) * | 2021-06-03 | 2021-09-03 | 常州一步干燥设备有限公司 | Condensation granulating device and process |
-
2017
- 2017-08-07 CN CN201720975988.2U patent/CN207025261U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113332925A (en) * | 2021-06-03 | 2021-09-03 | 常州一步干燥设备有限公司 | Condensation granulating device and process |
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