CN203389569U - Air-float type blending tank device - Google Patents
Air-float type blending tank device Download PDFInfo
- Publication number
- CN203389569U CN203389569U CN201320456498.3U CN201320456498U CN203389569U CN 203389569 U CN203389569 U CN 203389569U CN 201320456498 U CN201320456498 U CN 201320456498U CN 203389569 U CN203389569 U CN 203389569U
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- main body
- blending tank
- air
- tank main
- blend tank
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- Expired - Fee Related
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- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
Abstract
The utility model discloses an air-float type blending tank device. The air-float type blending tank device comprises a blending tank main body, wherein two groups of air flushing circular rings are arranged at the bottom of the blending tank main body; a vacuum compressor is arranged below the blending tank main body; the two groups of air flushing circular rings are connected with the vacuum compressor through pipelines. During blending of pine oil, materials can be fully mixed and move integrally to form homogeneous phase liquid. Therefore, the sampling results are always the same every time or at every point, thus ensuring stability of detection results and yield of products.
Description
Technical field
The utility model relates to pine tar production technical field, is specifically related to air floatation type blend tank device.
Background technology
The production of pine tar can directly be produced, and also can be deployed into by terpinol and dipentene etc. the pine tar of different content., in the process of allotment pine tar, be wherein all generally with pump, to beat circulation a period of time again after the product of allotment is extracted into blend tank, then just sampling detects.But beat in cyclic process at pump, material can form the loop from import to outlet in blend tank, the both sides in Zhe Tiao loop are just difficult to most identify oneself with the process of circulation away from more far from center, loop, even can form position, dead angle, therefore allot the pine tar coming also easily inhomogeneous, cause the accuracy of detection unstable, be unfavorable for carrying out smoothly of subsequent handling.
Utility model content
The utility model has solved the problem that prior art exists, and a kind of air floatation type blend tank device is provided.
The utility model is achieved by the following technical programs:
Air floatation type blend tank device, comprises blend tank main body, and described blend tank bottom part body is provided with two groups of qi of chong channel ascending adversely annulus, and blend tank main body below is provided with vacuum compression device simultaneously.
Wherein, two groups of qi of chong channel ascending adversely annulus are all connected with vacuum compression device by pipeline.Qi of chong channel ascending adversely annulus can pass through vacuum compression device external compressed air.
In addition, be all arranged with many group air admission holes on every group of qi of chong channel ascending adversely annulus, described air admission hole external diameter is 3mm.
The utility model usefulness is:
The utility model can make material fully mix in the allocation process of pine tar, make all material mass motions, form homogeneous liquid, therefore the sampling result of every sub-sampling or each point is the same, ensure the stable of testing result, also contributed to ensure the yield of product.
Accompanying drawing explanation
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail:
Fig. 1 is structure chart of the present utility model.
The specific embodiment
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein is only in order to explain the utility model, and be not used in restriction the utility model.
Be illustrated in figure 1 the air floatation type blend tank device that can be used as the utility model preferred embodiment, comprise blend tank main body 1, described blend tank main body 1 bottom is provided with two groups of qi of chong channel ascending adversely annulus 2, and blend tank main body 1 below is provided with vacuum compression device 4 simultaneously.
Wherein, two groups of qi of chong channel ascending adversely annulus 2 are all connected with vacuum compression device 4 by pipeline.
In addition, be all arranged with many group air admission holes 3 on every group of qi of chong channel ascending adversely annulus 2, described air admission hole 3 external diameters are 3mm.
In actual production, the quantity of qi of chong channel ascending adversely annulus 2 can be adjusted to three groups or more than, simultaneously its external diameter need coordinate the base diameter of blend tank main body 1.After all materials are added to blend tank main body 1, by vacuum compression device 4, toward qi of chong channel ascending adversely annulus 2, be blown into gas, gas enters blend tank main body 1 through each air admission hole 3, now the interior all materials of blend tank main body 1 will form rolling from top to bottom, rolling process continues after general 20 minutes, and the material in tank just can mix completely.And as adopted pump to play circulation, generally want within 1 hour, just can substantially reach above-mentioned effect above.
Claims (1)
1. air floatation type blend tank device, comprises blend tank main body (1), it is characterized in that described blend tank main body (1) bottom is provided with two groups of qi of chong channel ascending adversely annulus (2), and blend tank main body (1) below is provided with vacuum compression device (4) simultaneously; Wherein, two groups of qi of chong channel ascending adversely annulus (2) are all connected with vacuum compression device (4) by pipeline; In addition, be all arranged with many group air admission holes (3) on every group of qi of chong channel ascending adversely annulus (2), described air admission hole (3) external diameter is 3mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320456498.3U CN203389569U (en) | 2013-07-29 | 2013-07-29 | Air-float type blending tank device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320456498.3U CN203389569U (en) | 2013-07-29 | 2013-07-29 | Air-float type blending tank device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203389569U true CN203389569U (en) | 2014-01-15 |
Family
ID=49901132
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320456498.3U Expired - Fee Related CN203389569U (en) | 2013-07-29 | 2013-07-29 | Air-float type blending tank device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203389569U (en) |
-
2013
- 2013-07-29 CN CN201320456498.3U patent/CN203389569U/en not_active Expired - Fee Related
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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: 20140115 Termination date: 20170729 |