CN205412294U - Continuous foam fractionation separation and purification tower and air jet system thereof - Google Patents
Continuous foam fractionation separation and purification tower and air jet system thereof Download PDFInfo
- Publication number
- CN205412294U CN205412294U CN201521077306.3U CN201521077306U CN205412294U CN 205412294 U CN205412294 U CN 205412294U CN 201521077306 U CN201521077306 U CN 201521077306U CN 205412294 U CN205412294 U CN 205412294U
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- CN
- China
- Prior art keywords
- air jet
- fumarole
- jet
- jet system
- tower
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- 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
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Abstract
The utility model provides a continuous foam fractionation separation and purification tower and air jet system thereof, the air jet system includes jet head and jet -propelled tube connector, the jet head last, jet -propelled tube connector down, jet head and the tube connector that spouts pass through screw thread swivelling joint, jet -propelled tube connector bottom is gaseous and introduces the mouth, the jet head is discoid, is thickness 0.1 10cm, it has a plurality of fumarole to open on the jet head, the fumarole in bank is arranged on the jet head surface, is the aperture of fumarole 0.1 5mm, the trompil direction of fumarole is the trompil inclination with the inclination of horizontal plane, is the trompil inclination 15 90 the degree, is round interval between per two rows of fumaroles 0.05 2cm. The atmosphere liquor ratio surface of bubble can be guaranteed to bloat by this air jet system, can guarantee the speed of continuous defoaming again, effectual improvement separation and purification efficiency.
Description
Technical field
The utility model relates to a kind of continuous foam rectifying separating-purifying tower and air jet system thereof.
Background technology
Bubble washes one's hair rectifying process for separation and purification continuously; it is based on table (boundary) face physics and attached principle; purification surface-active and a kind of new separation technology of on-surface-active material is concentrated as separating medium by bubble; the most constantly it is widely used in the industrial production of scale; such as the separation of protein, enzyme, virus etc. and purification in biological medicine engineering; textile printing and dyeing wastewater processes; the extraction of gentamicin; food additives and the separation of preservative and purification; aquaculture water processes, etc..
The air jet system of continuous foam rectifying separating-purifying tower has the inert gas of certain pressure for bubbling, and its foam size produced and uniformity coefficient are to ensure that the key factor of separating-purifying efficiency.
Summary of the invention
Problem to be solved in the utility model is the air jet system of a kind of continuous foam rectifying separating-purifying tower, both can guarantee that the maximum gas liquid ratio surface bloating bubble, and can guarantee that again the speed of continuous froth breaking, effective raising separating-purifying efficiency.
For solving above-mentioned technical problem, the technical solution adopted in the utility model is: the air jet system of a kind of continuous foam rectifying separating-purifying tower, it is characterized in that: described air jet system includes jet thrust and air jet pipe connector, described jet thrust upper, air jet pipe connector under, jet thrust and air jet pipe connector are connected by screw thread rotation, effectively reach gas to be evenly distributed, gas-tight, it is ensured that the generation of uniform bubble.
It is gas introduction port bottom described air jet pipe connector；Described jet thrust is discoid, and thickness is 0.1-10cm；Having several fumaroles on described jet thrust, described fumarole arranged in rows is on jet thrust surface；The aperture of described fumarole is 0.1-5mm；The perforate direction of fumarole and the inclination angle of horizontal plane are perforate inclination angle, and described perforate inclination angle is 15-90 degree；Round spacing between every two row's fumaroles is 0.05-2cm.
Further, the closer to the fumarole in the center of circle, its perforate inclination angle is closer to 90 degree；The closer to its perforate inclination angle of fumarole at edge closer to 15 degree.
Further, the cross section of described air jet pipe connector is funnel-form.
Preferably, the fumarole area of described jet thrust upper surface and to account for the ratio of the upper surface gross area be 1%-50%.
Preferably, described jet thrust thickness is 2cm.
Preferably, the aperture of described fumarole is 2mm.
Preferably, described round spacing is 1cm.
The present invention also provides for a kind of continuous foam rectifying separating-purifying tower, and including foam fractionation tower, described foam fractionation tower bottom is provided with air jet system, and side Ta Bi is provided with charging aperture, is provided with residual solution outlet bottom opposite side tower wall；Described foam fractionation top of tower and a foam bed conduit are connected, and the other end of described foam bed conduit connects a froth breaker, and described froth breaker top is provided with defoamer entrance, and bottom is provided with discharging opening.
The utility model has the advantage that with good effect: the parameters of careful design air jet system, guarantee the generation of uniform bubble, control the bubble bubble diameter of homogeneous distribution, generation is of moderate size and the uniform bubble of bubble diameter, to reach maximum gas liquid ratio surface, ensure the speed of continuous froth breaking, it is possible to be effectively improved separating-purifying efficiency simultaneously.
Accompanying drawing explanation
Fig. 1 is the main TV structure schematic diagram of the air jet system of the utility model continuous foam rectifying separating-purifying tower
Fig. 2 is the plan structure schematic diagram of the air jet system of the utility model continuous foam rectifying separating-purifying tower
Fig. 3 is the schematic diagram of the utility model continuous foam rectifying separating-purifying tower
In figure:
1, jet thrust；2, air jet pipe connector；3, gas introduction port；4, fumarole；5, foam fractionation tower；6, air jet system；7, charging aperture；8, residual solution outlet；9, foam bed conduit；10, froth breaker；11, defoamer entrance；12, discharging opening.
Detailed description of the invention
Embodiment 1
A kind of air jet system of continuous foam rectifying separating-purifying tower, including jet thrust 1 and air jet pipe connector 2, jet thrust 1 upper, air jet pipe connector 2 under, jet thrust 1 and air jet pipe connector 2 are connected by screw thread rotation, effectively reach gas to be evenly distributed, gas-tight, it is ensured that the generation of uniform bubble.
It it is gas introduction port 3 bottom air jet pipe connector 2；Jet thrust 1 is discoid, and thickness H is 0.1-10cm；Having several fumaroles 4 on jet thrust 1, fumarole 4 arranged in rows is on jet thrust 1 surface；The aperture of fumarole 4 is 0.1-5mm；The perforate direction of fumarole 4 and the inclination angle of horizontal plane are perforate inclination angle, and perforate inclination angle is 15-90 degree；The closer to the fumarole 4 in the center of circle, its perforate inclination angle is closer to 90 degree；The closer to its perforate inclination angle of fumarole 4 at edge closer to 15 degree.Round spacing h between every two row's fumaroles 4 is 0.05-2cm.The fumarole area of jet thrust 4 upper surface and the ratio accounting for the upper surface gross area are 1%-50%.
Embodiment 2
A kind of continuous foam rectifying separating-purifying tower, including foam fractionation tower 5, is provided with air jet system 6 bottom foam fractionation tower 5, side Ta Bi is provided with charging aperture 7, is provided with residual solution outlet 8 bottom opposite side tower wall；Foam fractionation tower 5 top is connected with a foam bed conduit 9, and the other end of foam bed conduit 9 connects a froth breaker 10, and froth breaker 10 top is provided with defoamer entrance 11, and bottom is provided with discharging opening 12.
The material needing rectifying enters foam fractionation tower 5 from charging aperture 7, converge with the inert gas foam sprayed from air jet system 6, inert gas foam enters foam bed on material and leads 9 pipes from top, through froth breaker 10, defoamer enters from defoamer entrance 11, material after purification, after froth breaking, flows out from discharging opening 12, obtains concentrating and purifying product.
Above embodiment of the present utility model is described in detail, but described content has been only preferred embodiment of the present utility model, it is impossible to be considered the practical range for limiting the present invention.All impartial changes made according to the utility model scope and improvement etc., within all should still belonging to this patent covering scope.
Claims (8)
1. the air jet system of a continuous foam rectifying separating-purifying tower, it is characterised in that: described jet fills
Put and include jet thrust and air jet pipe connector, described jet thrust upper, air jet pipe connector under, jet
Head and air jet pipe connector are connected by screw thread rotation, introduce for gas bottom described air jet pipe connector
Mouthful；Described jet thrust is discoid, and thickness is 0.1-10cm；Several sprays are had on described jet thrust
Pore, described fumarole arranged in rows is on jet thrust surface；The aperture of described fumarole is 0.1-5mm；
The perforate direction of fumarole and the inclination angle of horizontal plane are perforate inclination angle, and described perforate inclination angle is 15-90 degree；
Round spacing between every two row's fumaroles is 0.05-2cm.
The air jet system of continuous foam rectifying separating-purifying tower the most according to claim 1, its feature
Being: the closer to the fumarole in the center of circle, its perforate inclination angle is closer to 90 degree；Jet the closer to edge
Its perforate inclination angle, hole is closer to 15 degree.
The air jet system of continuous foam rectifying separating-purifying tower the most according to claim 1, its feature
It is: the cross section of described air jet pipe connector is funnel-form.
The air jet system of continuous foam rectifying separating-purifying tower the most according to claim 1, its feature
It is: the fumarole area of described jet thrust upper surface and the ratio accounting for the upper surface gross area are 1%-50%.
The air jet system of continuous foam rectifying separating-purifying tower the most according to claim 1, its feature
It is: described jet thrust thickness is 2cm.
The air jet system of continuous foam rectifying separating-purifying tower the most according to claim 1, its feature
It is: the aperture of described fumarole is 2mm.
The air jet system of continuous foam rectifying separating-purifying tower the most according to claim 1, its feature
It is: described round spacing is 1cm.
8. include a continuous foam rectifying separating-purifying tower for air jet system described in claim 1-7,
It is characterized in that: include that foam fractionation tower, described foam fractionation tower bottom are provided with described air jet system, one
Side Ta Bi is provided with charging aperture, is provided with residual solution outlet bottom opposite side tower wall；Described foam fractionation tower top
Portion is connected with a foam bed conduit, and the other end of described foam bed conduit connects a froth breaker, described froth breaking
Device top is provided with defoamer entrance, and bottom is provided with discharging opening.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521077306.3U CN205412294U (en) | 2015-12-18 | 2015-12-18 | Continuous foam fractionation separation and purification tower and air jet system thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521077306.3U CN205412294U (en) | 2015-12-18 | 2015-12-18 | Continuous foam fractionation separation and purification tower and air jet system thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205412294U true CN205412294U (en) | 2016-08-03 |
Family
ID=56537913
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521077306.3U Expired - Fee Related CN205412294U (en) | 2015-12-18 | 2015-12-18 | Continuous foam fractionation separation and purification tower and air jet system thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205412294U (en) |
-
2015
- 2015-12-18 CN CN201521077306.3U patent/CN205412294U/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: 20160803 Termination date: 20201218 |