CN203598702U - Powdery material dissolution tank - Google Patents
Powdery material dissolution tank Download PDFInfo
- Publication number
- CN203598702U CN203598702U CN201320839961.2U CN201320839961U CN203598702U CN 203598702 U CN203598702 U CN 203598702U CN 201320839961 U CN201320839961 U CN 201320839961U CN 203598702 U CN203598702 U CN 203598702U
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- CN
- China
- Prior art keywords
- flour
- venturi tube
- tank body
- blender
- dissolving tank
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- Expired - Fee Related
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Abstract
The utility model discloses a powdery material dissolution tank which comprises a vertical tank body, wherein a material inlet is formed in the top of the vertical tank body; a material outlet is formed in the bottom of the vertical tank body; an external pipeline is arranged between the material outlet and the material inlet; a material pump, a mixer and a venturi tube are arranged on the external pipeline in sequence; a turbulent plate is welded on the inner wall of the mixer; an injection medium inlet of the venturi tube is connected with a powder pool. According to the powdery material dissolution tank, a powdery material is injected by virtue of the venturi tube and is fully mixed with water flow, so that powder is prevented from forming particles; in addition, the powdery material can be fully dissolved by virtue of the multistage expansion type mixer and the turbulent plate installed in the mixer.
Description
Technical field
The utility model relates to a kind of dissolution equipment, is specifically related to a kind of flour dissolving tank.
Background technology
In each production field, recycling after usually needing flour of all kinds to dissolve.Traditional dissolving method is very simple, is generally directly in container, to pack solvent and flour into, then adopts and manually stirs, and if desired container is heated.When production scale is large, meltage is when very large, usually there is dissolving the problems such as insufficient, labour intensity is large in this dissolving method.
Notification number is that the Chinese patent literature of CN201427025Y discloses a kind of dissolving tank, comprise tank body, described tank body is double-jacket, is a cavity between chuck, in cavity, be provided with heat(ing) coil, the entrance point of heat(ing) coil is connected with the heat source tube outside tank body, and tank body top is provided with transmission product pump, charging aperture and aproll ball, on transmission product pump, is connected with puddler, puddler stretches in tank body, tank body lower end is provided with sewage draining exit, and cavity upper end is provided with water inlet, and lower end is provided with discharge outlet and tail gas mouth.
Notification number is that the Chinese patent literature of CN201214732Y discloses a kind of dissolving tank, comprise tank body and be arranged on the agitator in tank body, agitator comprises shaft and is arranged on the stirring vane on shaft, on shaft, be provided with vertically at least two-layer stirring vane that comprises hinged joint layer blade and straight leaf layer blade, hinged joint layer blade is along the longitudinally folded plate type blade of bending of blade, straight leaf layer blade is Flat plate type blade, and all stirring vanes are all installed perpendicular to shaft.
Notification number is that the Chinese patent literature of CN202741060U discloses a kind of albumen powder dissolving tank, comprises tank body, is provided with paddle in tank body, and tank interior is provided with emulsification cutter, and emulsification cutter upper end is connected with tank body top.
Above-mentioned dissolving tank is all first flour and solvent all to be dropped in tank body, and agitating device or shear are set in tank body, stirs to overcome manpower the problem producing.But general dissolving tank volume is larger, and a large amount of flour drops into after solvent, very easily finishes, and forms particle, still there is the inhomogeneous problem of dissolving.
Utility model content
The utility model provides a kind of flour dissolving tank, and this dissolving tank utilizes Venturi tube injection flour to enter in solvent, guarantees to dissolve fully.
A kind of flour dissolving tank, comprise vertical tank body, the top of vertical tank body offers material inlet, bottom offers material outlet, between material outlet and material inlet, be provided with external pipe, on described external pipe, be provided with successively product pump, blender and Venturi tube, on the inwall of described blender, be welded with spoiler, the injection medium inlet of described Venturi tube is connected with pulvis pond.
In vertical tank body, fill in advance water, start product pump, water flows out and enters external pipe from material outlet; During through Venturi tube, in pipe, form low pressure, order about flour in pulvis pond and enter Venturi tube through pulvis conduit from injection medium inlet, sneaked in current by the flour of injection, enter in vertical tank body; Now the flour in feed liquid does not also all dissolve, feed liquid enters in the blender of tubular through material outlet, the barrel dliameter of blender is greater than the caliber of the tube connector that connects material outlet and blender, also be greater than the caliber of the tube connector that connects blender and Venturi tube, feed liquid enters after blender, be subject to after the flow-disturbing, shear action of spoiler, undissolved flour can obtain more fully and dissolve.
As preferably, export between material inlet in Venturi tube, described external pipe is also connected with pond by liquid conduits.So before dissolving only need vertical tank body in-built enter a small amount of water, synchronously water inlet in the process of injection pulvis, liquid conduits is arranged between Venturi tube outlet and material inlet, promotes mixing of current and flour.
As preferably, described spoiler is along blender circumferential equally distributed 3～5.
As preferably, described spoiler towards with the lopsidedness of Flow of Goods and Materials opposite direction.Increase spoiler to the shear action of dissolved substance not in feed liquid.
As further preferred, the angle between described spoiler and blender axis is 45～60 °.
As preferably, described blender is 2～4 that connect successively.Further making undissolved flour obtain more fully dissolves.
As preferably, between mixer outlet and Venturi tube entrance, on described external pipe, be provided with successively sampling pipe and discharge pipe.Sampling pipe is convenient to understand the dissolving situation of flour in feed liquid, if dissolve completely, from discharge pipe discharging.
In the utility model, described pulvis conduit, liquid conduits, sampling pipe, discharge pipe and material outlet place are equipped with valve.
Working method of the present utility model is:
In vertical tank body, pre-install a certain amount of water, start product pump, water flows out and enters external pipe from material outlet; During through Venturi tube, in pipe, form low pressure, order about flour in pulvis pond and enter Venturi tube through pulvis conduit from injection medium inlet, sneaked in current by the flour of injection, enter in vertical tank body, water also enters vertical tank body through liquid conduits simultaneously; Enter successively in multiple blenders through material outlet for fully dissolving feed liquid, be subject to flow-disturbing, the shear action of spoiler, undissolved flour obtains more fully and dissolves; The feed liquid of fully dissolving enters Venturi tube, continues injection flour and sneaks in feed liquid, in vertical tank body and external pipe, circulates; Reach after dissolving tank volume, close the valve of pulvis conduit and liquid conduits 4, after circulation several times, can dissolve situation through sampling pipe inspection, if fully dissolve, through discharge pipe discharging.
Compared with prior art, the beneficial effects of the utility model are:
The utility model utilizes Venturi tube injection flour, and flour is fully mixed with current, avoids occurring that powder forms the phenomenon of particle; And utilize the multistage blender expanding and be arranged on the spoiler in blender, impel the dissolving of flour more abundant.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of flour dissolving tank of the utility model.
The specific embodiment
As shown in Figure 1, a kind of flour dissolving tank of present embodiment, comprises vertical tank body 1, and the top of vertical tank body 1 offers material inlet, and bottom offers material outlet, is connected with external pipe 2 between material outlet and material inlet.
External pipe comprises the first vertical pipeline 21, the first horizontal pipe 22, the second vertical pipeline 23, the second horizontal pipe 24, the 3rd vertical pipeline 25 of series connection successively, the first vertical pipeline 21 is directly connected with material outlet and with valve, the product pump 3 that drives material to circulate is installed between the first vertical pipeline 21 and the first horizontal pipe 22 between vertical tank body 1 and external pipe 2.
On the first horizontal pipe 22, be furnished with the blender 27 of two tubulars of series connection successively, the barrel dliameter of blender 27 is greater than the caliber of the first horizontal pipe 22.On blender 27 inwalls, be provided with along having three spoilers 28 in circumferential equally distributed this specific embodiment of spoiler 28(of blender 27), and spoiler 28 towards with the lopsidedness of Flow of Goods and Materials opposite direction, the angle between spoiler 28 and blender 27 axis is preferably 45～60 ° (in this specific embodiment, being 60 °).
In blender 27 downstreams, on the first horizontal pipe 22, be also connected with sampling catheter 7 and material outlet canal 8, sampling catheter 7 and material outlet canal 8 are also with valve.
On the second horizontal pipe 24, be furnished with Venturi tube 26, Venturi tube 26 is connected with pulvis pond 6 by pulvis conduit 5; The 3rd vertical pipeline 25 is connected with pond (omitting in figure) by liquid conduits 4, and suction pump (omitting in figure) is installed on liquid conduits.Pulvis conduit 5 and liquid conduits 4 are also with valve.
Working method of the present utility model is:
At a certain amount of water of the interior prepackage of vertical tank body 1, open the valve on the first vertical pipeline 21, start product pump 3, water flows out from material outlet, enter successively the first vertical pipeline 21, the first horizontal pipe 22, the second vertical pipeline 23, the second horizontal pipe 24, when process is arranged in the Venturi tube 26 on the second horizontal pipe 24, in pipe, form low pressure, order about flour in pulvis pond 6 and enter Venturi tube 26 through pulvis conduit 5 from injection medium inlet, sneaked in current by the flour of injection, enter in vertical tank body 1, open suction pump simultaneously, water also enters vertical tank body 1 through liquid conduits 4,
The feed liquid of fully not dissolving flows out from material outlet again, enters in the blender 27 being arranged on the first horizontal pipe 22, is subject to flow-disturbing, the shear action of spoiler 28, and undissolved flour obtains more fully and dissolves; The feed liquid of fully dissolving enters Venturi tube 26, continues injection flour and sneaks in feed liquid, circulation in vertical tank body 1 and external pipe 2; Reach after dissolving tank volume, close the valve of pulvis conduit 5 and liquid conduits 4, after circulation several times, can check dissolving situation through sampling pipe 7, if fully dissolve, through discharge pipe 8 dischargings.
Claims (7)
1. a flour dissolving tank, comprise vertical tank body, the top of vertical tank body offers material inlet, bottom offers material outlet, it is characterized in that, between material outlet and material inlet, be provided with external pipe, on described external pipe, be provided with successively product pump, blender and Venturi tube, on the inwall of described blender, be welded with spoiler, the injection medium inlet of described Venturi tube is connected with pulvis pond.
2. flour dissolving tank as claimed in claim 1, is characterized in that, between Venturi tube outlet and material inlet, described external pipe is also connected with pond by liquid conduits.
3. flour dissolving tank as claimed in claim 1, is characterized in that, described spoiler is along blender circumferential equally distributed 3～5.
4. flour dissolving tank as claimed in claim 1, is characterized in that, described spoiler towards with the lopsidedness of Flow of Goods and Materials opposite direction.
5. want the flour dissolving tank as described in 4 as right, it is characterized in that, the angle between described spoiler and blender axis is 45～60 °.
6. flour dissolving tank as claimed in claim 1, is characterized in that, described blender is 2～4 that connect successively.
7. flour dissolving tank as claimed in claim 1, is characterized in that, between mixer outlet and Venturi tube entrance, is provided with successively sampling pipe and discharge pipe on described external pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320839961.2U CN203598702U (en) | 2013-12-18 | 2013-12-18 | Powdery material dissolution tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320839961.2U CN203598702U (en) | 2013-12-18 | 2013-12-18 | Powdery material dissolution tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203598702U true CN203598702U (en) | 2014-05-21 |
Family
ID=50711403
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320839961.2U Expired - Fee Related CN203598702U (en) | 2013-12-18 | 2013-12-18 | Powdery material dissolution tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203598702U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731914A (en) * | 2016-12-20 | 2017-05-31 | 中国石油天然气股份有限公司 | DDGS dissolver and DDGS dissolving method |
| CN108786509A (en) * | 2018-06-06 | 2018-11-13 | 哈尔滨万鑫石墨谷科技有限公司 | A kind of solid-liquid mixing device and method |
-
2013
- 2013-12-18 CN CN201320839961.2U patent/CN203598702U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731914A (en) * | 2016-12-20 | 2017-05-31 | 中国石油天然气股份有限公司 | DDGS dissolver and DDGS dissolving method |
| CN108786509A (en) * | 2018-06-06 | 2018-11-13 | 哈尔滨万鑫石墨谷科技有限公司 | A kind of solid-liquid mixing device and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140521 Termination date: 20171218 |