CN107281777A - Extraction reactor is crushed online - Google Patents
Extraction reactor is crushed online Download PDFInfo
- Publication number
- CN107281777A CN107281777A CN201710685672.4A CN201710685672A CN107281777A CN 107281777 A CN107281777 A CN 107281777A CN 201710685672 A CN201710685672 A CN 201710685672A CN 107281777 A CN107281777 A CN 107281777A
- Authority
- CN
- China
- Prior art keywords
- rotor
- extraction reactor
- online
- broken online
- bearing housing
- Prior art date
- 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.)
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/0215—Solid material in other stationary receptacles
- B01D11/0223—Moving bed of solid material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
Abstract
The invention provides a kind of extraction reactor broken online, including base and drive component, the drive component is arranged on the base, and the extraction reactor broken online also includes：Working chamber is provided with the first rotor and the second rotor, is spaced from each other between the first rotor and second rotor；Bearing housing is fixed on the base, and one end of the bearing housing is connected with one end of the working chamber, and the other end of the bearing housing is connected by main shaft with the drive component.Extraction reactor broken online of the invention is applied to high viscosity, the material of high solids content, these materials can efficiently be done work between the arc shaped blade of rotor, and by centrifugal action, outermost is thrown to by impeller central, moment enters efficiently to be mixed in the cavity of two rotors.The maximum speed of whole equipment is up to 3000rpm/min, operationally smooth running and noise is small.
Description
Technical field
The present invention relates to chemical field, more particularly to a kind of extraction reactor broken online, it is adaptable to petrochemical industry, pigment, dye
The industries such as material, coating, pharmacy, oil-water emulsion, fine chemistry industry, food and drink.
Background technology
The equipment that extraction reactor is often referred to liquid-liquid extraction.At present, used in domestic extraction reactor is at most centrifugation
Pump, gear pump, impeller pump, screw pump and membrane pump, but these equipment are had some limitations using upper.
For example, centrifugal pump and gear pump are adapted to the water or oil of conveying low viscosity, and impeller pump and screw pump can be conveyed
Cream kind material.Wherein, costly, the manufacture of screw pump is relatively rough for the price of impeller pump, is only applicable to low side industry.This
Outside, membrane pump is applied to the material conveying containing solid particle, but can not overcome pulse.
As can be seen here, the function of above-mentioned a few money pumps can only convey material, and applicable situation limits to.Therefore, this area skill
Art personnel urgently develop a kind of effective extraction reactor.
The content of the invention
The technical problem to be solved in the present invention be in order to overcome in the prior art extraction reactor have limited defect,
There is provided a kind of extraction reactor broken online, it is adaptable to high viscosity and the efficient mixing reactor of the high suspension of solid content.
The present invention is to solve above-mentioned technical problem by following technical proposals：
A kind of extraction reactor broken online, including base and drive component, the drive component are arranged on the base
On, its feature is, the extraction reactor broken online also includes：
It is provided with the first rotor and the second rotor in working chamber, the working chamber, the first rotor and described second turn
It is spaced from each other between son；
Bearing housing, the bearing housing is fixed on the base, and one end of the bearing housing and the one of the working chamber
End connection, the other end of the bearing housing is connected by main shaft with the drive component.
According to one embodiment of present invention, the first rotor is made up of 70 degree of left-handed blades of multi-disc.
According to one embodiment of present invention, the front end of the first rotor is equipped with end cap, and the end cap has 30 degree and inclined
Angle.
According to one embodiment of present invention, it is connected and fixed between the end cap and the first rotor by fixture.
According to one embodiment of present invention, it is set to arc Large Copacity inner chamber at the bitrochanteric feeding mouth.
According to one embodiment of present invention, the center on described bitrochanteric one side is provided with circular ring path, institute
State bitrochanteric another side and be provided with back of the body chamber, the circular ring path couples with the back of the body chamber.
According to one embodiment of present invention, the back of the body chamber is made up of six helical blades, the end of the helical blade
Couple tangent line discharging opening.
According to one embodiment of present invention, the drive component includes motor and transmission device, and the main shaft passes through institute
Stating motor drives the transmission device to realize rotation.
According to one embodiment of present invention, the transmission device is five groove Type B belt drive units.
According to one embodiment of present invention, between the first rotor and second rotor using between centers spacer every
Open.
The positive effect of the present invention is：
Extraction reactor broken online of the invention is applied to high viscosity, the material of high solids content, and these materials can turn
Efficiently done work between the arc shaped blade of son, and by centrifugal action, outermost is thrown to by impeller central, moment enters two turns
Efficiently mixed in the cavity of son.The liquid of impeller central can be set aside with very high speed, so that in impeller central shape
Into low pressure, working chamber collects from the liquid being spilled between each blade, can be thrown away along tangent line discharging opening, realizes high-order conveying.
The maximum speed of whole equipment is up to 3000rpm/min, operationally smooth running and noise is small.
Brief description of the drawings
The above and other feature of the present invention, property and advantage will pass through description with reference to the accompanying drawings and examples
And become apparent, identical reference represents identical feature all the time in the accompanying drawings, wherein：
Fig. 1 is the online structural representation for crushing extraction reactor of the present invention.
Fig. 2 is the sectional view splitted along line A-A in Fig. 1.
Fig. 3 is the online stereogram for crushing the first rotor in extraction reactor of the present invention.
Fig. 4 is the online front view for crushing the first rotor in extraction reactor of the present invention.
Fig. 5 is the online side view for crushing the first rotor in extraction reactor of the present invention.
Fig. 6 is the online stereogram for crushing the end cap of the first rotor in extraction reactor of the present invention.
Fig. 7 is the online front view for crushing the end cap of the first rotor in extraction reactor of the present invention.
Fig. 8 is the online side view for crushing the end cap of the first rotor in extraction reactor of the present invention.
Fig. 9 is bitrochanteric stereogram one in the present invention online broken extraction reactor.
Figure 10 is bitrochanteric stereogram two in the present invention online broken extraction reactor.
Figure 11 is bitrochanteric front view in the present invention online broken extraction reactor.
Figure 12 is bitrochanteric rearview in the present invention online broken extraction reactor.
Figure 13 is bitrochanteric side view in the present invention online broken extraction reactor.
Embodiment
For the above objects, features and advantages of the present invention can be become apparent, below in conjunction with tool of the accompanying drawing to the present invention
Body embodiment elaborates.
Embodiments of the invention are described with detailed reference to accompanying drawing now.Being preferable to carry out now with detailed reference to of the invention
Example, its example is shown in the drawings.In the case of any possible, in all of the figs identical will be used to mark to represent phase
Same or similar part.Although in addition, the term used in the present invention is selected from public term, originally
Some terms mentioned in description of the invention are probably that applicant carrys out selection by his or her judgement, and its detailed meanings is at this
Explanation in the relevant portion of the description of text.In addition, it is desirable to not only by used actual terms, and be also to by each
Meaning that term is contained understands the present invention.
Fig. 1 is the online structural representation for crushing extraction reactor of the present invention.Fig. 2 is the section view splitted along line A-A in Fig. 1
Figure.Fig. 3 is the online stereogram for crushing the first rotor in extraction reactor of the present invention.Fig. 4 is anti-for the online broken extraction of the present invention
Answer the front view of the first rotor in device.Fig. 5 is the online side view for crushing the first rotor in extraction reactor of the present invention.Fig. 6 is
The stereogram of the end cap of the first rotor in online broken extraction reactor of the invention.Fig. 7 crushes extractive reaction online for the present invention
The front view of the end cap of the first rotor in device.Fig. 8 is the online side for crushing the end cap of the first rotor in extraction reactor of the present invention
View.Fig. 9 is bitrochanteric stereogram one in the present invention online broken extraction reactor.Figure 10 is the online broken extraction of the present invention
Take bitrochanteric stereogram two in reactor.Figure 11 is bitrochanteric main view in the present invention online broken extraction reactor
Figure.Figure 12 is bitrochanteric rearview in the present invention online broken extraction reactor.Figure 13 is the online broken extraction of the present invention
Bitrochanteric side view in reactor.
As shown in figure 1 to figure 13, the invention discloses a kind of extraction reactor broken online, including base 10 and driving group
Part, the drive component is arranged on base 10.Wherein, the extraction reactor broken online also includes working chamber 20 and axle
Hold case 30.It is provided with working chamber 20 in the cavity of different-diameter, the cavity and is respectively arranged with the first rotor 21 and second turn
Son 22, will be spaced from each other between the rotor 22 of the first rotor 21 and second.For example, the rotor of the first rotor 21 and second in the present embodiment
Separated between 22 using between centers spacer.Bearing housing 30 is fixed on base 10, and one end of bearing housing 30 and the one of working chamber 20
End connection, and the other end of bearing housing 30 is connected by main shaft 31 with the drive component.
It is connected and sealed between bearing housing 30 and working chamber 20 by mechanical sealing assembly 32, forms an entirety.This
In mechanical seal use packaging type double mechanical seal.
In addition, bearing housing 30 here is double fulcrum supports, one end is fixed by one group of cylinder roller bearing, and the other end is by two
Group angular contact ball bearing is fixed.
The other end of working chamber 20 is provided with auxiliary material import 23 and major ingredient import 24, for being fed into working chamber 20
Operation.On the top of working chamber 20, one discharging opening 25 is set.
Preferably, the first rotor 21 is made up of 70 ° of left-handed blades 211 of multi-disc.End cap is housed in the front end of the first rotor 21
40, and end cap 40 has 30 ° of inclination angle.It is connected and fixed between end cap 40 and the first rotor 21 by fixture.Fixation herein
Part can be preferably four groups of a diameter of 8mm hexagon socket cap head screw.Multiple holes 41 are offered on the end face of end cap 40, so
It is attached to afterwards by hexagon socket cap head screw in hole 41 and the first rotor 21 is connected and fixed with end cap 40.
Preferably, it is set to arc Large Copacity inner chamber at the feeding mouth of the second rotor 22.On one side of the second rotor 22
Center is provided with circular ring path 221, and back of the body chamber 222 is provided with bitrochanteric another side so that circular ring path 221 and the back of the body
Chamber 222 couples.The diameter of circular ring path 221 herein can be preferably 17.5mm.Chamber 222 is carried on the back by six 223 groups of helical blades
Into, and the end connection tangent line discharging opening of helical blade 223.
Here the drive component mainly includes motor 50 and transmission device, and main shaft 31 drives the biography by motor 50
Dynamic device, which is realized, to be rotated.The transmission device is preferably five groove Type B belt drive units 60.In addition, also being set on base 10
It is equipped with machine envelope liquid storage compensator 70
Described according to said structure, after adopting the above technical scheme, the main shaft 31 of the online broken extraction reactor of the present invention
Drive five groove Type B belt drive units 60 to realize by motor 50 to rotate, maximum speed can reach 3000rpm/min.Make
During, the end cap 40 of high viscosity, the material of high solids content by charging aperture 24 along the first rotor 21 is brought into rapidly
The arc shaped blade of the first rotor 21.The blade end of the first rotor 21 and the unilateral gap of working chamber 20 are less than 2mm, so can be with
Force material efficiently to be done work between the arc shaped blade of the first rotor 21, and by centrifugal action, thrown to by impeller central
Outermost, is efficiently mixed so that moment enters in the cavity of two rotors.The high speed rotation of second rotor 22 forces impeller
The liquid at center is set aside with very high speed, so that in impeller central formation low pressure.So, when material reaches the second rotor 22
Impeller most peripheral when, flow velocity is very high.Working chamber 20 collects from the liquid being spilled between each blade, is got rid of along tangent line discharging opening
Go out.
In summary, broken extraction reactor is applied to high viscosity and the high suspension of solid content to the present invention online, is one
Plant high viscosity, high solids content, high-lift high-efficiency mixing device.Material can efficiently be done between the arc shaped blade of rotor
Work(, and by centrifugal action, outermost is thrown to by impeller central, moment enters efficiently to be mixed in the cavity of two rotors.
The liquid of impeller central can be set aside with very high speed, so that in impeller central formation low pressure, working chamber collects from each leaf
The liquid being spilled between piece, can throw away along tangent line discharging opening, realize high-order conveying.The maximum speed of whole equipment is reachable
3000rpm/min, operationally smooth running and noise is small.
Although the foregoing describing the embodiment of the present invention, it will be appreciated by those of skill in the art that these
It is merely illustrative of, protection scope of the present invention is defined by the appended claims.Those skilled in the art is not carrying on the back
On the premise of principle and essence from the present invention, various changes or modifications can be made to these embodiments, but these are changed
Protection scope of the present invention is each fallen within modification.
Claims (10)
1. a kind of extraction reactor broken online, including base and drive component, the drive component are arranged on the base,
Characterized in that, the extraction reactor broken online also includes：
Be provided with the first rotor and the second rotor in working chamber, the working chamber, the first rotor and second rotor it
Between be spaced from each other；
Bearing housing, the bearing housing is fixed on the base, and one end of the bearing housing and one end of the working chamber connect
Connect, the other end of the bearing housing is connected by main shaft with the drive component.
2. extraction reactor broken online as claimed in claim 1, it is characterised in that the first rotor is by 70 degree of left sides of multi-disc
Vane piece is constituted.
3. extraction reactor broken online as claimed in claim 2, it is characterised in that the front end of the first rotor is equipped with end
Lid, the end cap has 30 degree of inclination angles.
4. extraction reactor broken online as claimed in claim 3, it is characterised in that the end cap and the first rotor it
Between be connected and fixed by fixture.
5. extraction reactor broken online as claimed in claim 1, it is characterised in that set at the bitrochanteric feeding mouth
It is set to arc Large Copacity inner chamber.
6. extraction reactor broken online as claimed in claim 5, it is characterised in that the center on described bitrochanteric one side
Position is provided with circular ring path, and the bitrochanteric another side is provided with back of the body chamber, and the circular ring path couples with the back of the body chamber.
7. extraction reactor broken online as claimed in claim 6, it is characterised in that the back of the body chamber is by six helical blade sets
Into the end connection tangent line discharging opening of the helical blade.
8. extraction reactor broken online as claimed in claim 1, it is characterised in that the drive component includes motor and biography
Dynamic device, the main shaft drives the transmission device to realize and rotated by the motor.
9. extraction reactor broken online as claimed in claim 8, it is characterised in that the transmission device is five groove Type Bs
Belt drive unit.
10. the extraction reactor broken online as described in claim 1-9 any one, it is characterised in that the first rotor
Separated between second rotor using between centers spacer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710685672.4A CN107281777A (en) | 2017-08-11 | 2017-08-11 | Extraction reactor is crushed online |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710685672.4A CN107281777A (en) | 2017-08-11 | 2017-08-11 | Extraction reactor is crushed online |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107281777A true CN107281777A (en) | 2017-10-24 |
Family
ID=60105549
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710685672.4A Withdrawn CN107281777A (en) | 2017-08-11 | 2017-08-11 | Extraction reactor is crushed online |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107281777A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0312045A1 (en) * | 1987-10-13 | 1989-04-19 | Hitachi, Ltd. | Centrifugal extractor |
| WO2004018070A1 (en) * | 2002-08-26 | 2004-03-04 | Natex Prozesstechnologie Gesmbh | Method and device for the extraction of materials from liquids or solid dispersions |
| CN201416568Y (en) * | 2009-05-21 | 2010-03-03 | 上海俊乐制冷自控元件有限公司 | Drain pump impeller |
| CN102502568A (en) * | 2011-10-25 | 2012-06-20 | 瓮福（集团）有限责任公司 | Impeller phosphoric acid extractor |
| CN103470410A (en) * | 2013-09-30 | 2013-12-25 | 宋玉强 | Powerful rotating vortex air-oil mixture generator |
| CN106310993A (en) * | 2016-09-30 | 2017-01-11 | 合肥华运机械制造有限公司 | Pipeline type high shearing emulsification pump |
| CN207270760U (en) * | 2017-08-11 | 2018-04-27 | 上海弗鲁克科技发展有限公司 | Broken extraction reactor online |
-
2017
- 2017-08-11 CN CN201710685672.4A patent/CN107281777A/en not_active Withdrawn
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0312045A1 (en) * | 1987-10-13 | 1989-04-19 | Hitachi, Ltd. | Centrifugal extractor |
| WO2004018070A1 (en) * | 2002-08-26 | 2004-03-04 | Natex Prozesstechnologie Gesmbh | Method and device for the extraction of materials from liquids or solid dispersions |
| CN201416568Y (en) * | 2009-05-21 | 2010-03-03 | 上海俊乐制冷自控元件有限公司 | Drain pump impeller |
| CN102502568A (en) * | 2011-10-25 | 2012-06-20 | 瓮福（集团）有限责任公司 | Impeller phosphoric acid extractor |
| CN103470410A (en) * | 2013-09-30 | 2013-12-25 | 宋玉强 | Powerful rotating vortex air-oil mixture generator |
| CN106310993A (en) * | 2016-09-30 | 2017-01-11 | 合肥华运机械制造有限公司 | Pipeline type high shearing emulsification pump |
| CN207270760U (en) * | 2017-08-11 | 2018-04-27 | 上海弗鲁克科技发展有限公司 | Broken extraction reactor online |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20171024 |
|
| WW01 | Invention patent application withdrawn after publication |