CN208465886U - Circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice - Google Patents
Circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice Download PDFInfo
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- CN208465886U CN208465886U CN201820952489.6U CN201820952489U CN208465886U CN 208465886 U CN208465886 U CN 208465886U CN 201820952489 U CN201820952489 U CN 201820952489U CN 208465886 U CN208465886 U CN 208465886U
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- defeco
- tank
- full charge
- sulfitated juice
- juice
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Abstract
The utility model discloses circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice, reactor tank includes cylindrical tank body, and defeco-sulfitated juice entrance is provided at tank base center, and tank body is provided with the CO from top to bottom entered2Air inlet pipe, bubbler and multiple shunting gas-guide tubes, bubbler and CO2Air inlet pipe is connected with gas-guide tube is shunted；Bubbler is located on tank body central axis, and bubbler is circumferentially uniformly connected with multiple shunting gas-guide tubes in horizontal distribution, and the lower section for shunting gas-guide tube is evenly arranged with multiple convex teeth portions along gas-guide tube length direction is shunted, and offers gas outlet on convex teeth portion；Tank inner chamber bottom end is provided with centrum, and the center of centrum is provided in the axial direction with defeco-sulfitated juice access road.The purpose of this utility model is to provide circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice, existing overcome the shortcomings of that existing sulfitation process craft and full charge equipment lead to problems such as sulfurous method clarifying efficiency low to solve.
Description
Technical field
The utility model relates to carbon full charge technical fields of refining sugar, and in particular to circulation helical continous way is full in a kind of defeco-sulfitated juice
Fill reactor tank.
Background technique
Sugar manufacturing industry is that comparison is traditional and tended to the light industry of relative maturity, has had the history of centuries
?；According to the difference of sugaring cleaning technique, carbonatation process and sulfurous method can be divided into, carbonatation process clarifying efficiency is 25%~
40%, sulfurous method clarifying efficiency is 8%~15%；The clarifying efficiency of obvious sulfurous method can not compared with carbonatation process,
But carbonatation process clarification process needs a large amount of lime, production cost is higher, and generates the filter mud that can not largely recycle, and makes
At serious environmental pollution, carbon method production technology is caused to be controlled.Sulfurous method sugar refining technology is relative to carbonatation process sugaring work
Skill, the non-sugar impuritiess such as colloidal impurity, Polyphenols, iron ion in syrup are relatively more, it is difficult to completely remove, purification effect is lower.
In sulfurous method mixed juice contain the non-sugar of a large amount of impurity, to it is subsequent it is peace and quiet have a huge impact, directly affect product matter
Amount, white granulated sugar sulfur content produced is higher, and quality is relatively low, easily return color, non-shelf-stable, but in contrast sulfurous method due to
Have the characteristics that clarifying effect is stable, the processing that adapts to various sugarcane juices, sedimentation filtration are good, lower production costs and by each sugar
Factory generally uses.
Utility model content
The purpose of this utility model is to provide circulation helical continous way full charge reactor tanks in a kind of defeco-sulfitated juice, to solve
Overcome the shortcomings of that existing sulfitation process craft and full charge equipment lead to problems such as sulfurous method clarifying efficiency low.
To achieve the above object, the technical solution of the utility model are as follows:
Circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice, the reactor tank includes cylindrical tank body, institute
It states and is provided with defeco-sulfitated juice entrance at tank base center, tank body is provided with the CO from top to bottom entered2Air inlet pipe, bubbler and more
A shunting gas-guide tube, the bubbler and CO2Air inlet pipe is connected with gas-guide tube is shunted；The bubbler is located at tank body center
On axis, bubbler is circumferentially uniformly connected with multiple shunting gas-guide tubes in horizontal distribution, the lower section edge for shunting gas-guide tube
It shunts gas-guide tube length direction and is evenly arranged with multiple convex teeth portions, offer gas outlet on the convex teeth portion；The tank inner chamber
Bottom end is provided with centrum, and the center of centrum is provided in the axial direction with defeco-sulfitated juice access road.
Through the above technical solutions, the pure CO that tank body will be entered from top to bottom2Gas or boiler smoke pass through bubbler again
It is shunted gas-guide tube sufficiently to be hit, is being knocked into fine gas bubbles, most the gas outlet through convex teeth portion exports from top to bottom afterwards
Reverse circulation mixed convection is formed with the defeco-sulfitated juice entered from bottom to up, fine gas bubbles can more effectively be distributed to defeco-sulfitated juice
In, make its reacted with defeco-sulfitated juice more evenly, more sufficiently, more thoroughly, be conducive to fast and efficiently carry out full charge, make defeco-sulfitated juice with
It is 7.4~7.6 that quickly speed full charge, which is reacted to pH value,.
In one embodiment, the gas outlet is located at convex teeth portion least significant end.
Through the above technical solutions, hitting the gas come out from gas outlet adequately.
In one embodiment, the shunting gas-guide tube alongst extends to inner tank wall.
Through the above technical solutions, making CO2Export it is more comprehensive, make it more effectively mix touching with defeco-sulfitated juice
It hits, reaches more preferably full charge effect.
In one embodiment, it is uniformly arranged in the circumferential direction in the tank body there are six inclined plate, the inclined plate is to tank body bottom
Portion's inclination；The position of the inclined plate is higher than the installation site for shunting gas-guide tube.
Through the above technical solutions, inclined plate and tank base vertebral body structure can make defeco-sulfitated juice form eddy flow.In this way in and
Under the action of juice eddy flow, the fine gas bubbles being knocked are easier to be dispersed in defeco-sulfitated juice, not only accelerate reaction speed in this way, and
And the utilization rate of carbon dioxide is greatly improved, prevent the waste of carbon dioxide gas.
In one embodiment, diffuser is connected at the top of the tank body.
Through the above technical solutions, the exhaust gas in carbonating tank is discharged from top.
In one embodiment, the tank body top is provided with scattered bubbler.
Through the above technical solutions, being defoamed to the syrup of full charge knock-on reaction.
In one embodiment, the tank body lower side is provided with manhole.
Through the above technical solutions, people is entered in tank body by manhole carries out inspection and maintenance to tank in-vivo device.
In one embodiment, the tank body side is provided with the outlet of full charge juice.
Through the above technical solutions, the syrup that full charge is completed enters next process through the outlet of full charge juice.
In one embodiment, the bottom of the tank body is provided with slag-drip opening.
Through the above technical solutions, the sewage after cleaning in tank body is discharged from slag-drip opening after shutting down.
In one embodiment, the defeco-sulfitated juice access road is communicated with defeco-sulfitated juice supply line.
Through the above technical solutions, the neutralized juice supply line of the defeco-sulfitated juice for carrying out full charge, defeco-sulfitated juice entrance will be needed to lead to
Road enters in tank body.
The utility model has the advantages that
The utility model is with pure CO2Gas or flue gas are as clarifying agent, CO2Air inlet pipe from top to bottom enters bubbling
Device, then be bubbled down through shunting gas-guide tube, the neutralized juice access road of defeco-sulfitated juice enters past upstream behind carbonating tank middle position,
CO2It is reverse to flow to formation opposite with defeco-sulfitated juice flow direction, meanwhile, under the action of tank base vertebral body structure and inclined plate, CO2With in
With the blended absorbent of juice helically downflow type, to make defeco-sulfitated juice and CO2Absorbing reaction can be contacted well, and reaction is sufficiently equal
It is even, CO2Absorptivity is high, reaches 40%~45%, and required full charge liquid level is low, and volume is small, is not easy tank boil-overs, and the residence time is short, control
Stablize, generation granular calcium carbonate is more, to reach better full charge effect.Colloid various in defeco-sulfitated juice can preferably be removed
The non-sugar impuritiess such as impurity, Polyphenols, iron ion mention to achieve the purpose that ensure the well peace and quiet effect of syrup for subsequent workshop section
For better excellent syrup, the better high-quality commerieal sugar of output.
Detailed description of the invention
Fig. 1 is the front view of the utility model.
Fig. 2 is the utility model bubbler, the cooperation perspective view for shunting gas-guide tube.
Fig. 3 is the front view that the utility model shunts gas-guide tube.
Specific embodiment
The following examples illustrate the utility model, but is not intended to limit the scope of the present invention.
Embodiment 1
Circulation helical continous way full charge reactor tank includes cylindrical tank body 1 in a kind of defeco-sulfitated juice as shown in Figs. 1-3,
1 bottom center of tank body is provided with defeco-sulfitated juice entrance 2, and tank body 1 is provided with the CO from top to bottom entered2Air inlet pipe 3 is bubbled
Device 4 and multiple shunting gas-guide tubes 5, the bubbler 4 and CO2Air inlet pipe 3 is connected with gas-guide tube 5 is shunted；The bubbler 4
On 1 central axis of tank body, bubbler 4 is circumferentially uniformly connected with ten shunting gas-guide tubes 5 in horizontal distribution, the shunting
Gas-guide tube 5 alongst extends to 1 inner wall of tank body；The shunting gas-guide tube 5 includes straight sections 52 and convex teeth portion 51, described
Straight sections 52 and convex teeth portion 51 are integrally formed, and the lower section of the straight sections 52 for shunting gas-guide tube 5 is along 52 length direction of straight sections
Multiple convex teeth portions 51 are evenly arranged with, offer gas outlet 511 on the convex teeth portion 51；The gas outlet 511 is located at convex teeth portion
51 least significant ends.The gas for carrying out full charge reaction comes from pure CO2Gas or the carbon dioxide volume ratio of boiler flue flue gas generation are
The flue gas for being not required to processing of 12%-16%, the gas of large volume is through CO2Air inlet pipe 3 enters tank body 1 from top to bottom, in bubbler 4
Under the action of enter in the narrow shunting gas-guide tube straight sections 52 of internal diameter and hit into fine gas bubbles, fine gas bubbles are through convex
It obtains further hitting into more tiny microbubble when teeth portion, most the gas outlet through convex teeth portion exports from top to bottom afterwards, and ten
It shunts gas-guide tube 5 to be uniformly distributed circumferentially, the radially even distribution of multiple convex teeth portions 51, so that making CO2The more full side of export
Position, makes it more effectively carry out mixing collision with defeco-sulfitated juice, reaches more preferably full charge effect.
CO from top to bottom2Reverse circulation mixed convection, fine gas bubbles energy are formed with the defeco-sulfitated juice entered from bottom to up
It is more effectively distributed in defeco-sulfitated juice, reacts it with defeco-sulfitated juice more evenly, more sufficiently, more thoroughly, be conducive to fast and efficiently
Full charge is carried out, makes defeco-sulfitated juice with quickly speed full charge to pH value 7.4~7.6.In in the case where pH value is 7.4~7.6 adjusting
It is easier to cohesion occurs with non-sugar impuritiess such as colloidal impurity, Polyphenols, iron ions in juice and be removed, so that reaching ensures syrup
The purpose of good peace and quiet effect provides preferably excellent syrup for subsequent workshop section, the better high-quality commerieal sugar of output.
The 1 inner cavity bottom end of tank body is provided with centrum 6, and the center of centrum 6 is provided in the axial direction with defeco-sulfitated juice access road 7.
It is uniformly arranged in the circumferential direction in the tank body 1 there are six inclined plate 8, the inclined plate 8 is to 1 bottom angled of tank body；The position of the inclined plate 8
Higher than the installation site for shunting gas-guide tube 5.Inclined plate and tank base vertebral body structure can make defeco-sulfitated juice form eddy flow, in this way in and
Under the action of juice eddy flow, the fine gas bubbles being knocked are easier to be dispersed in defeco-sulfitated juice, not only accelerate reaction speed in this way, and
And the utilization rate of carbon dioxide is greatly improved, prevent the waste of carbon dioxide gas.Constantly from defeco-sulfitated juice access road 7 into
Enter in tank body and mixed in the defeco-sulfitated juice of swirling motion and the subtle carbon dioxide gas progress spiral downflow type from gas outlet ejection
It closes and constantly rises, to make defeco-sulfitated juice and CO2Absorbing reaction can be contacted well, react full and uniform, CO2Absorptivity is high.Vertebra
The design of body 6 can also avoid walking short circuit into juice, avoid full charge circulation it is bad, exist stop dead angle the problems such as, reduce owe full charge
Or the phenomenon that overcarbonation, achieve the purpose that improve juice quality, reduces evaporation incrustation, reduces energy consumption.
The top of the tank body 1 is connected with diffuser 9, and the exhaust gas in carbonating tank is discharged from top.
1 top of tank body is provided with scattered bubbler 10, defoams to the syrup of full charge knock-on reaction.
1 lower side of tank body is provided with manhole 11, and people is entered in tank body by manhole checks tank in-vivo device
And maintenance.
1 side of tank body is provided with full charge juice outlet 12, the most of effect in pump of the syrup of full charge knock-on reaction
It is lower to be taken away through full charge juice outlet 12, enter settling vessel after having heated.
The bottom of the tank body 1 is provided with slag-drip opening 13, after shutdown, to the sewage after cleaning in tank body from slag-drip opening
Discharge.
Defeco-sulfitated juice supply line 14 is connected on the tank body 1, the defeco-sulfitated juice supply line 14 and defeco-sulfitated juice entrance are logical
Road 7 communicates.
Sulfurous method clarification is carried out using the carbonating tank, clarifying efficiency reaches 15% or more, juice calcium salt content
0.35% hereinafter, color value of clear juice (900IU) juice and mixed 1.2% or more juice purity difference, juice turbidity 5%, the residual sulphur drop of juice
30%, the residual sulphur drop 40% of filtered juice, the defeco-sulfitated juice sedimentation time can put juice at 36 minutes, and the filtered juice sedimentation time 22 minutes put juice, most
Whole white granulated sugar sulfur content without Syrup Flotation can control 20 milligrams hereinafter, about using controllable 10 milligrams of Syrup Flotation sulfur content with
Under, it is fully solved white granulated sugar brightness reversion problem, the storage of finished product white granulated sugar the time limit 3 years or more, fried sugar value changed less in 10~30IU
Left and right, market distant view are splendid.
Although above having made detailed description to the utility model with generality explanation and specific embodiment,
On the basis of the utility model, it can be made some modifications or improvements, this is apparent to those skilled in the art
's.Therefore, these modifications or improvements on the basis of without departing from the spirit of the present invention, belong to the utility model and want
Seek the range of protection.
Claims (10)
1. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice, which is characterized in that the reactor tank includes cylindrical
Tank body (1), tank body (1) bottom center is provided with defeco-sulfitated juice entrance (2), and tank body (1), which is provided with, from top to bottom to be entered
CO2Air inlet pipe (3), bubbler (4) and multiple shunting gas-guide tubes (5), the bubbler (4) and CO2Air inlet pipe (3) and shunting
Gas-guide tube (5) is connected；The bubbler (4) is located on tank body (1) central axis, and bubbler (4) is circumferentially uniformly connected with
Multiple shunting gas-guide tubes (5) in horizontal distribution, the lower section for shunting gas-guide tube (5) is along shunting gas-guide tube (5) length direction
It is evenly arranged with multiple convex teeth portions (51), offers gas outlet (511) on the convex teeth portion (51)；The interior bottom of chamber of the tank body (1)
End is provided with centrum (6), and the center of centrum (6) is provided in the axial direction with defeco-sulfitated juice access road (7).
2. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice as described in claim 1, which is characterized in that it is described go out
Port (511) is located at convex teeth portion (51) least significant end.
3. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice as described in claim 1, which is characterized in that described point
Conductance tracheae (5), which alongst extends to, contradicts tank body (1) inner wall.
4. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice as described in claim 1, which is characterized in that the tank
It is uniformly arranged in the circumferential direction in body (1) there are six inclined plate (8), the inclined plate (8) is to tank body (1) bottom angled；The inclined plate (8)
Position is higher than the installation site for shunting gas-guide tube (5).
5. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice as described in claim 1, which is characterized in that the tank
Diffuser (9) are connected at the top of body (1).
6. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice as described in claim 1, which is characterized in that the tank
Body top is provided with scattered bubbler (10).
7. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice as described in claim 1, which is characterized in that the tank
Body (1) lower side is provided with manhole (11).
8. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice as described in claim 1, which is characterized in that the tank
Body (1) side is provided with full charge juice outlet (12).
9. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice as described in claim 1, which is characterized in that the tank
The bottom of body (1) is provided with slag-drip opening (13).
10. circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice as described in claim 1, which is characterized in that described
It is connected on tank body (1) defeco-sulfitated juice supply line (14), the defeco-sulfitated juice supply line (14) and defeco-sulfitated juice access road (7) phase
It is logical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820952489.6U CN208465886U (en) | 2018-06-20 | 2018-06-20 | Circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820952489.6U CN208465886U (en) | 2018-06-20 | 2018-06-20 | Circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208465886U true CN208465886U (en) | 2019-02-05 |
Family
ID=65214394
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820952489.6U Expired - Fee Related CN208465886U (en) | 2018-06-20 | 2018-06-20 | Circulation helical continous way full charge reactor tank in a kind of defeco-sulfitated juice |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208465886U (en) |
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2018
- 2018-06-20 CN CN201820952489.6U patent/CN208465886U/en not_active Expired - Fee Related
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190205 Termination date: 20200620 |
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| CF01 | Termination of patent right due to non-payment of annual fee |