CN207371534U - Neutralization reactor with agitating function - Google Patents
Neutralization reactor with agitating function Download PDFInfo
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- CN207371534U CN207371534U CN201721362692.XU CN201721362692U CN207371534U CN 207371534 U CN207371534 U CN 207371534U CN 201721362692 U CN201721362692 U CN 201721362692U CN 207371534 U CN207371534 U CN 207371534U
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- jet pipe
- short tube
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- flow short
- pipe
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Abstract
The utility model belongs to neutralization reactor apparatus field, is related to a kind of neutralization reactor with agitating function, and including reaction babinet, top is equipped with upper nozzle in reaction chamber body, and lower part is equipped with lower nozzle；Upper nozzle includes upper jet pipe, one end of upper jet pipe is connected by upper connector, the side of upper jet pipe the same side is equipped with jet flow short tube, the central axes of upper jet flow short tube and the angled setting of horizontal direction, the upper connector upper end of upper nozzle connects upper delivery pipe by beam barrel, and the relatively upper delivery pipe of upper nozzle is freely rotated；Lower nozzle includes lower jet pipe, one end of lower jet pipe is connected by lower connector, the side of lower jet pipe the same side is equipped with lower jet flow short tube, central axes and the angled setting of horizontal direction of lower jet flow short tube, and the lower connector lower end of lower nozzle connects lower delivery pipe by beam barrel.The structure design of the utility model is reasonable, and upper nozzle and lower nozzle form rotation under the reaction force of fluid, so as to which liquid in container be driven to rotate, reaches mixing effect.
Description
Technical field
The utility model is related to a kind of neutralization reactors with agitating function, belong to neutralization reactor apparatus field.
Background technology
In the chemical processes such as ammonia synthesis, methanol-fueled CLC, preparing ethylene glycol, it usually needs heat exchange is carried out using reactor,
And carry out chemosynthesis reaction.In the reactor, various material needs are sufficiently mixed, and chemical reaction can carry out fully.Mesh
Before, the nozzle for conveying material is fixed, stirring is can not achieve in reactor, therefore the material in reactor has reaction
Insufficient phenomenon, there are greater losses for material.
Utility model content
The purpose of this utility model is that propose a kind of neutralization reactor with agitating function, the neutralization with agitating function
The upper nozzle and lower nozzle of reactor form rotation under the reaction force of fluid, so as to which liquid in container be driven to rotate, most
Achieve the effect that stirring eventually.
Neutralization reactor described in the utility model with agitating function, including reaction babinet, top is set in reaction chamber body
There is upper nozzle, upper nozzle includes several upper jet pipes, and one end of upper jet pipe is connected by upper connector, and each upper jet pipe is evenly distributed with
It is set in upper connector surrounding in divergence expression, the side of each upper jet pipe the same side is equipped with jet flow short tube, upper jet flow short tube
It is set along the radial direction of upper jet pipe, and the central axes of upper jet flow short tube are set with horizontal direction angled one, the upper company of upper nozzle
Junctor upper end connects upper delivery pipe by beam barrel, and the relatively upper delivery pipe of upper nozzle is freely rotated；Lower part is equipped with down in reaction chamber body
Nozzle, lower nozzle include several lower jet pipes, and one end of lower jet pipe is connected by lower connector, and each lower jet pipe is distributed on down
Connector surrounding is set in divergence expression, and the side of each lower jet pipe the same side is equipped with lower jet flow short tube, and lower jet flow short tube is under
The radial direction of jet pipe is set, and the central axes of lower jet flow short tube are set with horizontal direction angled two, the lower connector of lower nozzle
Lower end connects lower delivery pipe by beam barrel, and lower nozzle descends delivery pipe to be freely rotated relatively.
In use, material one enters upper nozzle by upper delivery pipe, and then material one enters upper jet pipe, then passes through upper spray
Short tube is flowed to spray into reaction chamber body, while material two enters lower nozzle by lower delivery pipe, and then material two enters lower jet pipe, so
It is sprayed into afterwards by lower jet flow short tube in reaction chamber body.Upper nozzle and lower nozzle are respectively in the reaction of two jet flow of material one and material
Rotation is formed under power, achievees the effect that be stirred to react material in babinet.Upper delivery pipe and lower delivery pipe play conveying material simultaneously
With the effect of two nozzles of support.
Preferably, the upper jet pipe side equipped with upper jet flow short tube is with the lower jet pipe side equipped with lower jet flow short tube
Different directions side.Therefore, the direction of rotation of upper nozzle and lower nozzle is on the contrary, can make material mixing more uniform.
Preferably, the upper jet pipe and lower jet pipe are horizontally disposed, and upper jet flow short tube is obliquely installed obliquely, lower jet flow
Short tube is obliquely installed obliquely, makes two kinds of material contacts abundant.
Preferably, the quantity of the upper jet pipe and lower jet pipe is 2-10.
Preferably, the quantity of the lower jet flow short tube of the described every upper jet flow short tube for going up jet pipe and every lower jet pipe is 3-
15。
Preferably, being circular layout in the reaction chamber body has several baffle plates, and each baffle plate is set along box height direction
It puts, one end of baffle plate is connected fixation with inner wall, and baffle plate can change the flow direction of material, can make two kinds of material mixing
More uniformly.
Preferably, the quantity of the baffle plate is 6-16.
Preferably, the angle one and angle two are 20 ° -80 °.
Possessed advantageous effect is the utility model compared with prior art：
The structure design of the utility model is reasonable, and upper nozzle and lower nozzle form rotation under the reaction force of fluid, from
And liquid in container is driven to rotate, it is finally reached the effect of stirring；And baffle plate is equipped in reaction chamber body, baffle plate can also
Mix material more uniform.
Description of the drawings
Fig. 1, the neutralization reactor structural representation front view with agitating function；
Fig. 2, the neutralization reactor structural representation top view with agitating function.
In figure：1st, babinet is reacted；2nd, upper delivery pipe；3rd, beam barrel；4th, lower jet flow short tube；5th, lower nozzle；6th, lower delivery pipe；7、
Upper jet flow short tube；8th, upper nozzle；9th, baffle plate；10th, upper jet pipe；11st, lower jet pipe.
Specific embodiment
The utility model is described further below in conjunction with the accompanying drawings：
Such as Fig. 1 and Fig. 2, the neutralization reactor described in the utility model with agitating function, including reacting babinet 1, reaction
1 internal upper part of babinet is equipped with upper nozzle 8, and upper nozzle 8 includes several upper jet pipes 10, and one end of upper jet pipe 10 is connected by upper connector
It is logical, and each upper jet pipe 10 is distributed on connector surrounding and is set in divergence expression, and the side of each upper 10 the same side of jet pipe is all provided with
There is upper jet flow short tube 7, upper jet flow short tube 7 is set along the radial direction of upper jet pipe 10, and the central axes of upper jet flow short tube 7 and level side
It is set to angled one, the upper connector upper end of upper nozzle 8 connects upper delivery pipe 2, the relatively upper conveying of upper nozzle 8 by beam barrel 3
Pipe 2 is freely rotated；React babinet 1 in lower part be equipped with lower nozzle 5, lower nozzle 5 include several lower jet pipes 11, the one of lower jet pipe 11
End is connected by lower connector, and each lower jet pipe 11 is distributed on lower connector surrounding and is set in divergence expression, each lower jet pipe 11
The side of the same side is equipped with lower jet flow short tube 4, and lower jet flow short tube 4 is set along the radial direction of lower jet pipe 11, and lower jet flow short tube 4
Central axes and horizontal direction angled two set, the lower connector lower end of lower nozzle 5 connects lower delivery pipe 6 by beam barrel 3, under
Nozzle 5 descends delivery pipe 6 to be freely rotated relatively.
In the present embodiment：10 side of upper jet pipe equipped with upper jet flow short tube 7 and 11 side of lower jet pipe equipped with lower jet flow short tube 4
Face is different directions side, and therefore, the direction of rotation of upper nozzle 8 and lower nozzle 5 is on the contrary, can make material mixing more uniform；
Upper jet pipe 10 and lower jet pipe 11 are horizontally disposed, and upper jet flow short tube 7 is obliquely installed obliquely, and lower jet flow short tube 4 tilts obliquely
It sets；The quantity of upper jet pipe 10 and lower jet pipe 11 is 4, and the quantity of the upper jet flow short tube 7 of every upper jet pipe 10 is 7, is sprayed under every
The quantity for flowing short tube 4 is 5；Reaction 1 annular of babinet is disposed with several baffle plates 9, and each baffle plate 9 is set along box height direction
It puts, one end of baffle plate 9 is connected fixation with inner wall, and the quantity of baffle plate 9 is 8, and baffle plate 9 can make two kinds of material mixing more
Add uniformly；Angle one and angle two are 45 °.
In use, material one enters upper nozzle 8 by upper delivery pipe 2, and then material one enters upper jet pipe 10, then passes through
Upper jet flow short tube 7 is sprayed into reaction babinet 1, while material two enters lower nozzle 5 by lower delivery pipe 6, and then material two enters
Then lower jet pipe 11 is sprayed by lower jet flow short tube 4 in reaction babinet 1.Upper nozzle 8 and lower nozzle 5 are respectively in material one and object
Expect to form rotation under the reaction force of two jet flows, and the direction of rotation of upper nozzle 8 and lower nozzle 5 is stirred to react on the contrary, reaching
The effect of material in babinet 1, in the process, baffle plate 9 change the flow direction of material, mix two kinds of materials more equal
It is even.Upper delivery pipe 2 and lower delivery pipe 6 play the role of conveying material simultaneously and support two nozzles.
Claims (8)
1. a kind of neutralization reactor with agitating function, including reaction babinet (1), it is characterised in that：React babinet (1) internal upper part
Equipped with upper nozzle (8), upper nozzle (8) includes several upper jet pipes (10), and one end of upper jet pipe (10) is connected by upper connector,
And each upper jet pipe (10) is distributed on connector surrounding and is set in divergence expression, and the side of each upper jet pipe (10) the same side is all provided with
There is upper jet flow short tube (7), upper jet flow short tube (7) is set along the radial direction of upper jet pipe (10), and the central axes of upper jet flow short tube (7)
Angled with horizontal direction one is set, and the upper connector upper end of upper nozzle (8) passes through delivery pipe (2) in beam barrel (3) connection, upper spray
The relatively upper delivery pipe (2) of head (8) is freely rotated；It reacts babinet (1) interior lower part and is equipped with lower nozzle (5), lower nozzle (5) includes several
Jet pipe (11) under root, one end of lower jet pipe (11) is connected by lower connector, and each lower jet pipe (11) is distributed on lower connector
Surrounding is set in divergence expression, and the side of each lower jet pipe (11) the same side is equipped with lower jet flow short tube (4), lower jet flow short tube (4)
It is set along the radial direction of lower jet pipe (11), and the central axes of lower jet flow short tube (4) are set with horizontal direction angled two, lower nozzle
(5) lower connector lower end connects lower delivery pipe (6) by beam barrel (3), and lower nozzle (5) descends delivery pipe (6) to be freely rotated relatively.
2. the neutralization reactor according to claim 1 with agitating function, it is characterised in that：Equipped with upper jet flow short tube (7)
Upper jet pipe (10) side with equipped with lower jet flow short tube (4) lower jet pipe (11) side be different directions side.
3. the neutralization reactor according to claim 2 with agitating function, it is characterised in that：Upper jet pipe (10) and lower jet pipe
(11) horizontally disposed, upper jet flow short tube (7) is obliquely installed obliquely, and lower jet flow short tube (4) is obliquely installed obliquely.
4. the neutralization reactor according to claim 1 with agitating function, it is characterised in that：Upper jet pipe (10) and lower jet pipe
(11) quantity is 2-10.
5. the neutralization reactor according to claim 1 with agitating function, it is characterised in that：Jet pipe (10) is upper on every
The quantity of the lower jet flow short tube (4) of jet flow short tube (7) and every lower jet pipe (11) is 3-15.
6. the neutralization reactor according to claim 1 with agitating function, it is characterised in that：React babinet (1) annular
Several baffle plates (9) are disposed with, each baffle plate (9) is set along box height direction, and one end of baffle plate (9) is connected admittedly with inner wall
It is fixed.
7. the neutralization reactor according to claim 6 with agitating function, it is characterised in that：The quantity of baffle plate (9) is
6-16。
8. the neutralization reactor with agitating function according to claim 1 or 3, it is characterised in that：Angle one and angle two
For 20 ° -80 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721362692.XU CN207371534U (en) | 2017-10-20 | 2017-10-20 | Neutralization reactor with agitating function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721362692.XU CN207371534U (en) | 2017-10-20 | 2017-10-20 | Neutralization reactor with agitating function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207371534U true CN207371534U (en) | 2018-05-18 |
Family
ID=62336675
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721362692.XU Active CN207371534U (en) | 2017-10-20 | 2017-10-20 | Neutralization reactor with agitating function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207371534U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110002635A (en) * | 2019-04-30 | 2019-07-12 | 宁波渤川废液处置有限公司 | Waste alkali liquor treatment device |
-
2017
- 2017-10-20 CN CN201721362692.XU patent/CN207371534U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110002635A (en) * | 2019-04-30 | 2019-07-12 | 宁波渤川废液处置有限公司 | Waste alkali liquor treatment device |
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