CN201643993U - Steam mixed heating type material dissolving tank - Google Patents
Steam mixed heating type material dissolving tank Download PDFInfo
- Publication number
- CN201643993U CN201643993U CN2010201460404U CN201020146040U CN201643993U CN 201643993 U CN201643993 U CN 201643993U CN 2010201460404 U CN2010201460404 U CN 2010201460404U CN 201020146040 U CN201020146040 U CN 201020146040U CN 201643993 U CN201643993 U CN 201643993U
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- steam
- tank
- dissolving
- jar
- tank body
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Abstract
The utility model relates to a container, and aims to provide a steam mixed heating type material dissolving tank, which comprises a tank body and a stirrer arranged in the tank body, and is characterized in that a steam inlet is arranged on a tank cover, a steam inlet pipe and a steam loop are arranged in the tank body, and the steam inlet pipe is connected with a steam inlet and the steam loop; and the steam loop is positioned at a tank bottom, and a plurality of small steam outlet holes which are towards different directions are evenly distributed along the periphery of the steam loop. When the product is used for dissolving material, steam is guided by the steam inlet pipe, is ejected from the small steam outlet holes on the loop of the dissolving tank bottom, is mixed and condensed with solution, provides heat for dissolving the material, and speeds up the dissolving process. When dissolving is carried out, a motor drives the stirrer to rotate, and an agitating vane pushes liquid to move towards a tank wall to form circulation in the tank, and thereby the dissolving is speeded up. Simultaneously, a baffle of the inner wall of the tank makes the liquid form vortex more easily, so the dissolving process in the tank is accelerated.
Description
Technical field
The utility model relates to a kind of container, particularly is used to prepare the material dissolution jar that the solute dissolving needs the solution of heat absorption (as urea granules).
Background technology
The dissolving of some material is to need heat absorption.When the solution of these materials of preparation, solute dissolving needs a large amount of heat absorptions, as no thermal source heating will cause the hurried decline of solution temperature, phenomenon appearance such as dissolution velocity is slack-off, dissolving is incomplete.For the solution preparation of these materials, need when preparation, heat often solution.Mostly existing mode of heating is electrical heating or at dissolving tank heater is set to utilize external thermal source heating.These two kinds of mode of heatings all belong to indirect, exist certain heat transfer resistance between thermal source and solution, the heating weak effect, and it is higher to make complicated cost.The present invention proposes a kind of steam that utilizes as thermal source, steam is directly fed the apparatus that solution carries out material dissolution.
The utility model content
Problem to be solved in the utility model is that a kind of material dissolution jar of vapor mixing heated type is provided.This dissolving tank dissolved urea etc. fast needs the material of heating, and dissolving completely, and required stirring motor power is low.
The utility model solves this technical problem the technical scheme that is adopted:
A kind of material dissolution jar of vapor mixing heated type is provided, comprise tank body and be arranged on the interior agitator of tank body, it is characterized in that, establish the steam inlet on the cover, steam is set in the tank body introduces conduit and steam loop, steam is introduced conduit and is connected steam inlet and steam loop; At the bottom of steam loop was positioned at jar, its circumference uniform distribution plurality of opening was towards the steam (vapor) outlet aperture of different directions.
As a kind of improvement, some baffle plates are set on the inner tank wall.
As a kind of improvement, described baffle plate is arranged symmetrically on the inner tank wall.
As a kind of improvement, described baffle plate is vertically mounted on the inner tank wall, and extends to cover at the bottom of jar.
As a kind of improvement, the width of described baffle plate is 1/10～1/20 of a tank body internal diameter, leaves the gap between baffle plate and the tank skin.
As a kind of improvement, thermometer hole is set on described tank body or the cover, observes manhole, discharging hole, taphole, steam inlet, liquid level gauge mouth, material inlet, solvent inlet and drain.
As a kind of improvement, described agitator comprises the stirring motor that is arranged on the cover, and stirring motor connects shaft, and the shaft end is established stirring vane.
The beneficial effects of the utility model are:
When this product was used for material dissolution, steam was introduced conduit by steam and is introduced, and a plurality of steam (vapor) outlet apertures ejections from the endless tube that is arranged in the dissolving tank bottom, with the solution condensation by mixing, for material dissolution provides institute's calorific requirement, accelerated course of dissolution.Motor-driven agitator rotation during dissolving, stirring vane promotes liquid and forms circulation in the jar to the tank skin motion, promotes dissolving.The baffle plate of jar inwall makes the easier formation eddy current of liquid simultaneously, makes a jar interior course of dissolution accelerate.
Description of drawings
Fig. 1 is a batching dissolving tank cutaway view of the present utility model;
Fig. 2 is the vertical view (having removed stirring motor) of Fig. 1;
Fig. 3 is the vertical view of steam loop;
Fig. 4 is the cutaway view at A-A place among Fig. 3;
Fig. 5 is the cutaway view at B-B place among Fig. 3.
Be denoted as 1 tank body, 2 steam inlets, 3 liquid level gauge mouths, 4 stirring motors, 5 solute imports among the figure, 6 baffle plates, 7 thermometer mouths, 8 stirring vanes, 9 observe manhole, 10 discharging holes, 11 steam loops, 12 tapholes, 13 solvent inlets, 14 drains, 15 steam (vapor) outlet apertures.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is further specified.
As depicted in figs. 1 and 2, the utility model dissolving tank comprises tank body 1 and the agitator and the steam loop 11 that are arranged in the tank body 1, and agitator comprises shaft and the stirring vane 8 that is installed on the shaft, stirring vane is generally 4, and length is 1/3 of dissolving tank diameter; The dissolving tank inwall generally is provided with 4 baffle plates 6, baffle plate 6 be vertically mounted on the dissolving tank skin on and at the bottom of jar, extend to the top, width normally tank diameter 1/10 to 1/12.Can leave tank skin for moderately viscous solution and put baffle plate, form the stagnant wake in case contact part with baffle plate at tank skin; The baffle plate that full-bodied solution is used should tilt to put, and barrier width is reduced to 1/20 of tank diameter.Overlook and observe the dissolving tank of preparing burden, when stirring motor drove the shaft rotation, stirring vane 8 made liquid move to tank skin, thereby made solution form a jar interior circulation, and the baffle plate 6 on the tank skin makes solution form eddy current simultaneously, allows solute dissolve in the solvent more equably.Also greatly reduce simultaneously the energy consumption of stirring motor.
As depicted in figs. 1 and 2, tank body also can be provided with thermometer mouth 7, observe manhole 9, discharging hole 10 and taphole 12, and thermometer is installed can detected temperatures, the solution temperature of control batching dissolving tank; Observe manhole and be used for the maintenance jar; Discharging hole is used to get rid of waste residue; Taphole is used for the solution that configures is failed away.
As shown in Figure 2, cover is provided with steam inlet 2, liquid level gauge mouth 3, solute import 5, solvent inlet 13 and drain 14.The liquid level gauge mouth is equipped with magnetic turnover panel liquid level gauge, is used to grasp solution height, the ingredients solution jar height change when promptly the height of input solvent is transported to storage tank with the solution for preparing by pump before the batching.
To shown in Figure 5, the utility model batching dissolving tank has steam that thermal source is provided as Fig. 3.Evenly have the aperture of different directions on the steam loop, steam enters in the solution by the steam (vapor) outlet in the steam loop 11 15, and by rising to liquid level at the bottom of the jar, heat is fully absorbed by solution, and solution temperature is raise, and allows solute dissolve fast.The endless tube uphill process of steam at the bottom of the jar, form gas-liquid mixed, reduced the resistance of liquid, so also improved stirring efficiency with solution.
It is also to be noted that what more than enumerate only is specific embodiment of the utility model.Obviously, the utility model is not limited to above embodiment, and many distortion can also be arranged.All distortion that those of ordinary skill in the art can directly derive or associate from the disclosed content of the utility model all should be thought protection domain of the present utility model.
Claims (7)
1. the material dissolution jar of a vapor mixing heated type, comprise tank body and be arranged on the interior agitator of tank body, it is characterized in that, establish the steam inlet on the cover, steam is set in the tank body introduces conduit and steam loop, steam is introduced conduit and is connected steam inlet and steam loop; At the bottom of steam loop was positioned at jar, its circumference uniform distribution plurality of opening was towards the steam (vapor) outlet aperture of different directions.
2. material dissolution jar according to claim 1 is characterized in that, some baffle plates are set on the inner tank wall.
3. material dissolution jar according to claim 2 is characterized in that described baffle plate is arranged symmetrically on the inner tank wall.
4. material dissolution jar according to claim 2 is characterized in that described baffle plate is vertically mounted on the inner tank wall, and extends to cover at the bottom of jar.
5. material dissolution jar according to claim 2 is characterized in that, the width of described baffle plate is 1/10～1/20 of a tank body internal diameter, leaves the gap between baffle plate and the tank skin.
6. according to described any one material dissolution jar of claim 1 to 5, it is characterized in that, thermometer hole is set on described tank body or the cover, observes manhole, discharging hole, taphole, steam inlet, liquid level gauge mouth, material inlet, solvent inlet and drain.
7. according to described any one material dissolution jar of claim 1 to 5, it is characterized in that described agitator comprises the stirring motor that is arranged on the cover, stirring motor connects shaft, and the shaft end is established stirring vane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201460404U CN201643993U (en) | 2010-03-30 | 2010-03-30 | Steam mixed heating type material dissolving tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201460404U CN201643993U (en) | 2010-03-30 | 2010-03-30 | Steam mixed heating type material dissolving tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201643993U true CN201643993U (en) | 2010-11-24 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201460404U Expired - Lifetime CN201643993U (en) | 2010-03-30 | 2010-03-30 | Steam mixed heating type material dissolving tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201643993U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102226041A (en) * | 2011-05-25 | 2011-10-26 | 苏州龙英织染有限公司 | Dye dispersion device |
| CN102614791A (en) * | 2012-03-30 | 2012-08-01 | 神华集团有限责任公司 | Dissolving device |
| CN102872759A (en) * | 2012-09-14 | 2013-01-16 | 横店集团浙江英洛华硅材料有限公司 | Heat energy recycling system for alkalization kettle |
| CN103170280A (en) * | 2013-04-03 | 2013-06-26 | 江阴华美数码科技有限公司 | Coating agent burdening structure |
| CN106139939A (en) * | 2016-04-21 | 2016-11-23 | 福建漳州久依久化工有限公司 | A kind of device and method utilizing the water-soluble material of steam jet ejector heating for dissolving |
| CN107779264A (en) * | 2017-12-04 | 2018-03-09 | 李玉娟 | For extracting the vapor can of fruits and vegetables essential oil |
| CN113230915A (en) * | 2021-06-16 | 2021-08-10 | 周伟 | Energy-saving urea dissolving tank heat cyclic utilization system |
-
2010
- 2010-03-30 CN CN2010201460404U patent/CN201643993U/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102226041A (en) * | 2011-05-25 | 2011-10-26 | 苏州龙英织染有限公司 | Dye dispersion device |
| CN102226041B (en) * | 2011-05-25 | 2013-06-05 | 苏州龙英织染有限公司 | Dye dispersion device |
| CN102614791A (en) * | 2012-03-30 | 2012-08-01 | 神华集团有限责任公司 | Dissolving device |
| CN102872759A (en) * | 2012-09-14 | 2013-01-16 | 横店集团浙江英洛华硅材料有限公司 | Heat energy recycling system for alkalization kettle |
| CN103170280A (en) * | 2013-04-03 | 2013-06-26 | 江阴华美数码科技有限公司 | Coating agent burdening structure |
| CN106139939A (en) * | 2016-04-21 | 2016-11-23 | 福建漳州久依久化工有限公司 | A kind of device and method utilizing the water-soluble material of steam jet ejector heating for dissolving |
| CN107779264A (en) * | 2017-12-04 | 2018-03-09 | 李玉娟 | For extracting the vapor can of fruits and vegetables essential oil |
| CN113230915A (en) * | 2021-06-16 | 2021-08-10 | 周伟 | Energy-saving urea dissolving tank heat cyclic utilization system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20101124 |
|
| CX01 | Expiry of patent term |