CN207254076U - A kind of band strengthens hybrid reaction and catches the full charge absorption tower of juice function - Google Patents
A kind of band strengthens hybrid reaction and catches the full charge absorption tower of juice function Download PDFInfo
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- CN207254076U CN207254076U CN201720787092.1U CN201720787092U CN207254076U CN 207254076 U CN207254076 U CN 207254076U CN 201720787092 U CN201720787092 U CN 201720787092U CN 207254076 U CN207254076 U CN 207254076U
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Abstract
A kind of band strengthens hybrid reaction and catches the full charge absorption tower of juice function, including tower body, juice catching device, polylith overflow plate, juice flow inlet, air intake, exhaust outlet, arrange juice mouth and agitating device, the exhaust outlet is arranged on tower body top, the juice catching device is arranged on below exhaust outlet, the polylith overflow plate layering is alternately arranged on below juice catching device, the juice flow inlet is arranged on the tower body between juice catching device and the superiors' overflow plate, the air intake is arranged on the tower body below orlop overflow plate, it is the liquid storage tank part of tower body below the air intake, agitating device is installed in the liquid storage tank, row's juice mouth is arranged on the tower body of liquid storage tank part.The utility model is provided with juice catching device; effectively prevent juice vapour from carrying some small droplets or drop containing sugar secretly and leaving tower body and cause the loss of sugar; it is subject to force to stir in the liquid storage tank of the latter half of the sugarcane juice in tower body so that carbon dioxide reacts more abundant with sugarcane juice, and efficiency greatly improves.
Description
Technical field
Sugar manufacturing machinery apparatus field is the utility model is related to, is specifically that a kind of band strengthens hybrid reaction and catches the full of juice function
Fill absorption tower.
Background technology
The peace and quiet technology of carbonatation process adds milk of lime and carbon dioxide in sugarcane juice and is set as main detergent, the main of use
Standby is carbonating tank.Carbon carbonating tank is the key equipment for clarifying process, whether full charge effect enough good have with device structure it is quite big
Relation, there are syrup to absorb CO for the carbonating tank of the prior art2Uneven, syrup easily occurs owing full charge or overcarbonation phenomenon, makes
Into evaporator incrustation amount it is more the problems such as.
Utility model content
The utility model is in view of the deficiencies of the prior art, there is provided a kind of band strengthens hybrid reaction and catches the full charge suction of juice function
Receive tower.
To achieve these goals, the utility model employs following technical scheme：
A kind of band strengthens hybrid reaction and catches the full charge absorption tower of juice function, including tower body, juice catching device, polylith overflow plate,
Juice flow inlet, air intake, exhaust outlet, row's juice mouth and agitating device,
The exhaust outlet is arranged on tower body top,
The juice catching device is arranged on below exhaust outlet,
The polylith overflow plate layering is alternately arranged on below juice catching device,
The juice flow inlet is arranged on the tower body between juice catching device and the superiors' overflow plate,
The air intake is arranged on the tower body below orlop overflow plate,
It is the liquid storage tank part of tower body below the air intake,
Agitating device is installed in the liquid storage tank,
Row's juice mouth is arranged on the tower body wall of liquid storage tank part.
Further, row's juice mouth is arranged at the bottom of liquid storage tank, and is connected with juice-ejecting tube, the height of juice-ejecting tube outlet
It is concordant with the design liquid level of liquid storage tank.
Further, the air intake is located between orlop overflow plate and the design liquid level of liquid storage tank.
Further, the agitating device drives rotating agitating paddle for motor.
Further, the agitating device is jet stirrer.
Further, the agitating device includes more set jet stirrers, and the jet exit of each set jet stirrer is opposite
Or the jet exit of each set jet stirrer is on the tangent line using tower center as the circle in the center of circle.
Further, the jet exit of more set jet stirrers is respectively positioned on below liquid level.
Further, the edge of the overflow plate is equipped with baffle.
Further, carbon dioxide concentrate device is further included, the carbon dioxide concentrate device includes tank body, exhaust pipe, air inlet
Pipe, condense water outlet and steam trap,
The outlet side of air inlet pipe is located at the top of tank body, and the inlet end of air inlet pipe is connected to sugar refinery flue gas sources；
The inlet end of exhaust pipe is arranged at the lower part of tank body, and the outlet side of exhaust pipe is connected to the air intake of tower body,
Condense water outlet and be located at the bottom of tank body, and be connected by pipeline with steam trap.
Further, buffering froth breaker is further included, row's juice mouth of the tower is connected with buffering froth breaker.
Compared with prior art, the beneficial effect that the utility model possesses：
(1) the utility model is provided with juice catching device, can come out the drop separation containing sugar from juice vapour so that containing liquid glucose
Drip back is flowed to inside tower body, effectively prevents juice vapour from carrying some small droplets or drop containing sugar secretly and leaving tower body and cause the damage of sugar
Lose.
(2) sugarcane juice constantly absorbs what is stepped up along overflow plate during tower body top half declines step by step along overflow plate
After carbon dioxide in flue gas, it is subject to force to stir in the liquid storage tank of the latter half in tower body so that carbon dioxide
React more abundant with sugarcane juice, efficiency greatly improves.
(3) the utility model can be matched with the existing flow sheet equipment of factory, and existing equipment can make full use of.This practicality
New no filter mud pollution, neutral or alkalescence can be with producing mixed fertilizer.The carbon dioxide of full charge comes from by separation
Boiler flue after reason, turns waste into wealth, and reduces the discharge capacity of boiler flue air carbon dioxide, reduces greenhouse effects, both ring
Protect energy saving, and emission reduction subtracts consumption.
Brief description of the drawings
Fig. 1 be agitating device described in the utility model be motor drive the band of rotating agitating paddle strengthen hybrid reaction and
Catch the structure diagram on the full charge absorption tower of juice function.
Fig. 2 is that the band that agitating device described in the utility model is jet stirrer strengthens hybrid reaction and catches juice function
The structure diagram on full charge absorption tower.
Fig. 3 is the schematic diagram of the opposite installation of jet exit of each set jet stirrer.
Fig. 4 is schematic diagram of the jet exit of each set jet stirrer along the tangent line installation of circle.
Fig. 5 is the structure of carbon dioxide concentrate device and its connection relationship diagram with tower body.
Embodiment
The technical solution of the utility model is further elaborated below by embodiment.
Embodiment 1
A kind of band strengthens hybrid reaction and catches the full charge absorption tower of juice function, including tower body 7, juice catching device 2, polylith overflow plate
4th, juice flow inlet 3, air intake 8, exhaust outlet 9, row's juice mouth 6 and agitating device,
The exhaust outlet 9 is arranged on 7 top of tower body,
The juice catching device 2 is arranged on the lower section of exhaust outlet 9,
The layering of polylith overflow plate 4 is alternately arranged on the lower section of juice catching device 2,
The juice flow inlet 3 is arranged on the tower body 7 between juice catching device 2 and the superiors' overflow plate 4,
The air intake 8 is arranged on the tower body 7 of the lower section of orlop overflow plate 4,
The lower section of air intake 8 is 9 part of liquid storage tank of tower body 7,
Agitating device is installed in the liquid storage tank 9,
Row's juice mouth 6 is arranged on the tower body 7 of 9 part of liquid storage tank.
Further, row's juice mouth 6 is arranged at the bottom of liquid storage tank 9, and is connected with juice-ejecting tube, the height of juice-ejecting tube outlet
Degree is concordant with the design liquid level of liquid storage tank 9.
Further, the air intake 8 is located between orlop overflow plate 4 and the highest liquid level of liquid storage tank 9.
Further, the agitating device drives rotating agitating paddle for motor.
Further, the agitating device is jet stirrer.
Further, the agitating device includes more set jet stirrers, and the jet exit of each set jet stirrer is opposite
Or the jet exit of each set jet stirrer is on the tangent line using tower center as the circle in the center of circle.
Further, the jet exit of more set jet stirrers is respectively positioned on below liquid level.
Further, the edge of the overflow plate 4 is equipped with baffle 5.
Further, further include carbon dioxide concentrate device, the carbon dioxide concentrate device include tank body 16, exhaust pipe 18,
Air inlet pipe 17, condense water outlet 19 and steam trap 20,
The outlet side of air inlet pipe 17 is located at the top of tank body 16, and the inlet end of air inlet pipe 17 is connected to sugar refinery flue gas sources；
The inlet end of exhaust pipe 18 is arranged at the lower part of tank body 16, and what the outlet side of exhaust pipe 18 was connected to tower body 7 enters gas
Mouth 8,
Condense water outlet 19 and be located at the bottom of tank body 16, and be connected by pipeline with steam trap 20.
Gas concentration lwevel in flue gas can bring up to 12 from 10~12% by the carbon dioxide concentrate device~
14%.
Further, buffering froth breaker 21 is further included, row's juice mouth 6 of the tower 7 is connected with buffering froth breaker 21, is used for
The bubble produced in the sugarcane juice after carbon strengthens full charge is eliminated, so as to the processing of subsequent processing.
Operation principle：
The edge of overflow plate 4 is equipped with baffle 5, is surrounded by overflow plate 4, baffle 5 and 7 wall of tower body into one with overflow
Plate 4 is bottom of pond using baffle 5 and 7 wall of tower body as the shallow pond of pool wall, and polylith overflow plate 4, which is layered alternately to set, refers to that polylith overflows
Flowing plate 4 is in tower body axial direction higher slice, and projection of the edge of upper strata overflow plate 4 on lower floor's overflow plate 4 is located at lower floor's overflow
The middle part of plate 4.Therefore, sugarcane juice enters in tower body 7 from juice flow inlet 3, then flows on the overflow plate 4 of the superiors, and sugarcane juice is from overflow
The edge of plate 4 is fallen on its next layer overflow plate 4 after crossing baffle 5, and so on, along each layer overflow plate 4 gradually
Fall, sugarcane juice is finally injected in liquid storage tank 9.
Carbon dioxide enters in tower body 7 from air intake 8, and the air intake 8 is arranged on the lower section of orlop overflow plate 4
On tower body 7, therefore carbon dioxide is needed since orlop overflow plate 4, crosses overflow plate 4 upwards step by step, and crossing
During, it is in contact and is dissolved in sugarcane juice with the sugarcane juice to flow downward, last tail gas is from the exhaust outlet for being arranged on 7 top of tower body
9 discharges.The waterfall that sugarcane juice is formed on overflow plates 4 at different levels and between overflow plate at different levels 4 causes the liquid level area of sugarcane juice to obtain
Increase to greatest extent.The air intake 8 is located between orlop overflow plate 4 and 11 height of highest liquid level of liquid storage tank 9, this is
Sugarcane juice is flowed out from air intake 8 in order to prevent.
The effect of juice catching device 2 for being arranged on the lower section of exhaust outlet 9 is will to contain liquid glucose drop from juice vapour to separate.
The juice flow inlet 3 is arranged on the tower body 7 between juice catching device 2 and the superiors' overflow plate 4, it is therefore an objective to ensures each piece
There can be sugarcane juice to flow through on overflow plate 4.
The lower section of air intake 8 is 9 part of liquid storage tank of tower body 7, and agitating device is provided with the liquid storage tank 9, is being overflow
Flowing plate 4 has partially absorbed the sugarcane juice of carbon dioxide, converges in 9 part of liquid storage tank, strengthens carbon dioxide and sugarcane by stirring
The reaction of juice.Row's juice mouth 6 is arranged on the tower body 7 of 9 part of liquid storage tank, and sugarcane juice after completion of the reaction leads to from row's juice mouth 6
Next workshop section.
Row's juice mouth 6 is arranged at the bottom of liquid storage tank 9, and is connected with juice-ejecting tube, the height and liquid storage of juice-ejecting tube outlet
The design liquid level in pond 9 is concordant.9 bottom of liquid storage tank is strengthened to the sugarcane juice for reacting and finishing using law of connected vessels to export in real time,
Meet the needs worked continuously.
The agitating device is jet stirrer.
Further, the agitating device includes more set jet stirrers, and the jet exit of each set jet stirrer is opposite
Or the jet exit of each set jet stirrer is on the tangent line using tower center as the circle in the center of circle.
Further, the jet exit of more set jet stirrers is respectively positioned on below liquid level.
As shown in figure 3, when respectively the jet exit of set jet stirrer is installed relatively, fluidic vectoring thrust percussion flow so that liquid storage
Liquid in pond 9 is fully flowed and mixed.
As shown in figure 4, respectively the jet exit of set jet stirrer is on the tangent line using tower center as the circle in the center of circle, respectively
A jet exit is set along clockwise at the same time, or each jet exit is set along counterclockwise at the same time, and each jet exit is penetrated
Mobilization force causes the liquid in liquid storage tank 9 to form whirlpool.
In figure, 14,15 be all the jet exit of jet stirrer.
A kind of implementation method of jet stirrer is：The sugarcane juice of liquid storage tank 9 is drawn using pipeline 12, by water pump 13
After pressurization, then inject in liquid storage tank 9.
Claims (10)
1. a kind of band strengthens hybrid reaction and catches the full charge absorption tower of juice function, it is characterised in that including tower body, juice catching device, more
Block overflow plate, juice flow inlet, air intake, exhaust outlet, row's juice mouth and agitating device,
The exhaust outlet is arranged on tower body top,
The juice catching device is arranged on below exhaust outlet,
The polylith overflow plate layering is alternately arranged on below juice catching device,
The juice flow inlet is arranged on the tower body between juice catching device and the superiors' overflow plate,
The air intake is arranged on the tower body below orlop overflow plate,
It is the liquid storage tank part of tower body below the air intake,
Agitating device is installed in the liquid storage tank,
Row's juice mouth is arranged on the tower body wall of liquid storage tank part.
2. band reinforcing hybrid reaction as claimed in claim 1 and the full charge absorption tower for catching juice function, it is characterised in that the row
Juice mouth is arranged at the bottom of liquid storage tank, and is connected with juice-ejecting tube, the height of juice-ejecting tube outlet and the design liquid level of liquid storage tank
Concordantly.
3. band reinforcing hybrid reaction as claimed in claim 1 and the full charge absorption tower for catching juice function, it is characterised in that it is described enter
Gas port is located between orlop overflow plate and the design liquid level of liquid storage tank.
4. band reinforcing hybrid reaction as claimed in claim 1 and the full charge absorption tower for catching juice function, it is characterised in that described to stir
Mix device and drive rotating agitating paddle for motor.
5. band reinforcing hybrid reaction as claimed in claim 1 and the full charge absorption tower for catching juice function, it is characterised in that described to stir
It is jet stirrer to mix device.
6. band reinforcing hybrid reaction as claimed in claim 5 and the full charge absorption tower for catching juice function, it is characterised in that described to stir
Mix device includes covering jet stirrers more, and each jet exit for covering jet stirrer is opposite or respectively covers the injection of jet stirrer
Outlet is on the tangent line using tower center as the circle in the center of circle.
7. band reinforcing hybrid reaction as claimed in claim 6 and the full charge absorption tower for catching juice function, it is characterised in that described more
The jet exit of set jet stirrer is respectively positioned on below liquid level.
8. band as claimed in claim 1 strengthens hybrid reaction and catches the full charge absorption tower of juice function, it is characterised in that described excessive
The edge of flowing plate is equipped with baffle.
9. the band as described in claim 1 ~ 8 any one strengthens hybrid reaction and catches the full charge absorption tower of juice function, its feature
It is, further include carbon dioxide concentrate device, the carbon dioxide concentrate device includes tank body, exhaust pipe, air inlet pipe, condensation water discharge
Mouth and steam trap,
The outlet side of air inlet pipe is located at the top of tank body, and the inlet end of air inlet pipe is connected to sugar refinery flue gas sources；
The inlet end of exhaust pipe is arranged at the lower part of tank body, and the outlet side of exhaust pipe is connected to the air intake of tower body,
Condense water outlet and be located at the bottom of tank body, and be connected by pipeline with steam trap.
10. band reinforcing hybrid reaction as claimed in claim 6 and the full charge absorption tower for catching juice function, it is characterised in that also wrap
Buffering froth breaker is included, row's juice mouth of the tower is connected with buffering froth breaker.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2017206567715 | 2017-06-07 | ||
| CN201720656771 | 2017-06-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207254076U true CN207254076U (en) | 2018-04-20 |
Family
ID=61926315
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720787092.1U Active CN207254076U (en) | 2017-06-07 | 2017-06-30 | A kind of band strengthens hybrid reaction and catches the full charge absorption tower of juice function |
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| Country | Link |
|---|---|
| CN (1) | CN207254076U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113385010A (en) * | 2021-05-10 | 2021-09-14 | 安徽省环境科学研究院 | System and method for capturing carbon dioxide in flue gas for power plant |
-
2017
- 2017-06-30 CN CN201720787092.1U patent/CN207254076U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113385010A (en) * | 2021-05-10 | 2021-09-14 | 安徽省环境科学研究院 | System and method for capturing carbon dioxide in flue gas for power plant |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230803 Address after: 530000 Guangxi Zhuang Autonomous Region Xixiangtang District Xiuling Road East Wuli Group 6 Community, Row 12, 20, 4th Floor, 2 Patentee after: GUANGXI KAIFAN INTELLIGENT TECHNOLOGY Co.,Ltd. Address before: No. 1701, Tower C, Tonghe Huiyuan Guanlan Pavilion, No. 89 Luban Road, Xixiangtang District, Nanning City, Guangxi Zhuang Autonomous Region, 530004 Patentee before: GUANGXI JUGUI TECHNOLOGY CO.,LTD. |
|
| TR01 | Transfer of patent right |