CN203174110U - Fast and efficient reverse carbonating tank - Google Patents
Fast and efficient reverse carbonating tank Download PDFInfo
- Publication number
- CN203174110U CN203174110U CN 201220738209 CN201220738209U CN203174110U CN 203174110 U CN203174110 U CN 203174110U CN 201220738209 CN201220738209 CN 201220738209 CN 201220738209 U CN201220738209 U CN 201220738209U CN 203174110 U CN203174110 U CN 203174110U
- Authority
- CN
- China
- Prior art keywords
- pot
- filling
- reverse
- fast
- carbonating tank
- 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.)
- Expired - Fee Related
Links
Abstract
The utility model discloses a fast and efficient reverse carbonating tank which belongs to the sugar industry. The fast and efficient reverse carbonating tank is characterized in that a CO2 gas inlet pipe entering from top to bottom is mounted in a cylinder body of the carbonating tank; an upper distribution plate is arranged in the middle of a carbonation apparatus, and a lower distribution plate is arranged at the cylinder-shaped bottom of the carbonating tank; an annular material distribution groove is formed between the upper distribution plate and the inner wall of the carbonation apparatus; an annular CO2 distribution pipe is arranged at the lower part of the lower distribution plate; a pre-lye entrance is formed in the carbonating tank from the middle part of the carbonating tank in a tangential way; and a main lime adding part is arranged at the upper part of a pre-lye pipe. According to the fast and efficient reverse carbonating tank, flow directions of CO2 and added lye are opposite, so that good circulation of mixed convection in reverse is formed, as a result, fast and efficient carbonation is realized, reaction is sufficient and uniform, absorption rate of CO2 is high, required liquid level for carbonation is low, volume is small, tank boil-overs is not easy, retention time is short, control is stable, more calcium carbonate particles are generated, and a better carbonation effect is achieved.
Description
Technical field
The utility model relates to the equipment that is applied to clarifying syrup in a kind of Closed Circulation in Sugar Production, especially a kind of reverse filling-up pot rapidly and efficiently.
Background technology
The syrup CO in present sugar refinery
2Full charge equipment generally is to be applied to the carbonatation process sugar refining technology, compares less and be applied to sulfurous method.The sulfurous method sugar refining technology is with respect to the carbonatation process sugar refining technology, and non-sugared impurity such as the colloidal impurity in the syrup, Polyphenols, iron ion are many, are difficult to remove fully, and purification effect is lower.Contain the non-sugar of a large amount of impurity in the sulfurous method mixing juice, to the very big influence of follow-up peace and quiet generation, directly influence quality product, and the CO of sulfurous method mixing juice
2Full charge compares less, the CO of existing mixing juice
2Full charge is the novel method of sulfurous method sugar refining technology.
Summary of the invention
In order to overcome the deficiency of existing sulfitation process craft and full charge equipment, the utility model provides a kind of reverse filling-up pot rapidly and efficiently, and this filling-up pot can solve the deficiency of sulfurous method cleaning technique well; Can remove impurity insolubles in the sulfurous method mixing juice again, guarantee the purpose of the good peace and quiet effect of syrup, for subsequent handling provides better good syrup.
The technical scheme that its technical problem that solves the utility model adopts is: CO
2Inlet pipe from top to bottom enters into the distribution endless tube, adds lye and tangentially enter CO in the middle of filling-up pot
2Gas adds lye and enter the back to dirty, CO in the middle of jar from distribution endless tube bubbling up
2Thereby up with add lye and contact to the convection current of dirty formation backmixing.Add lye and in reverse, fully absorb CO
2, reaction generates granular calcium carbonate, removes from the bottom slag removing hole when precipitation lime-ash that produces is shut down, and the gas of generation is discharged from the diffuser at top.
Constitutional features is: a kind of reverse filling-up pot rapidly and efficiently comprises that top is the filling-up pot of round shape, lower taper, is characterized in that: the CO that from top to bottom enters is housed in the filling-up pot cylindrical shell
2Inlet pipe, last grid distributor is located at the centre of full charge device, and following grid distributor is located at the columnar bottom of filling-up pot, and the cloth annular groove is located between grid distributor and the full charge device inwall, CO
2The distribution endless tube is located at down under the grid distributor, and the predefecation juice entrance tangentially enters into filling-up pot from the mid-way of filling-up pot, and the master adds the top that the ash place is located at the predefecation juice pipe.
The cloth annular groove is metal cylinder, is welded on the filling-up pot inwall, is on the same level attitude with last grid distributor.
The master who is located at predefecation juice pipe top adds Hui Chu and last grid distributor is level attitude, is connected to the outside of filling-up pot.
CO
2Inlet pipe is passed the outer wall of filling-up pot to the middle part, and palintrope is along to the endless tube that distributes, with the distribution rings sealing of tube together.
The beneficial effects of the utility model are: by grid distributor about in the of two filling-up pot is divided into three parts, CO
2Inlet pipe from top to bottom enters into the distribution endless tube, by following grid distributor bubbling up, adds lye and tangentially enters behind the filling-up pot mid-way toward dirty CO
2Flow to add the opposite formation of the lye flow direction reverse, add lye and CO
2Can well contact absorption reaction, sufficient reacting is even, CO
2The specific absorption height, required full charge liquid level is low, and volume is little, is difficult for tank boil-overs, and the residence time is short, and control is stable, and it is more to generate granular calcium carbonate, thereby reaches better full charge effect.Can better remove non-sugared impurity such as adding colloidal impurities various in the lye, Polyphenols, iron ion, thereby reach the purpose of guaranteeing the good peace and quiet effect of syrup, for follow-up workshop section provides better good syrup, the better high-quality commerieal sugar of output.
Description of drawings
Fig. 1 is the utility model structural representation.
Among the figure: 1. reverse filling-up pot rapidly and efficiently, 2. diffuser is 3. gone up manhole, 4. jar in ladder, 5. cloth annular groove, grid distributor is 7. gone up in 6. full charge juice outlet, 8. juice outlet groove 9. descends grid distributor, 10. CO
2The distribution endless tube, 11. row's end mouths, 12. slag removing holes, 13. times manholes, 14. predefecation juice entrances, 15. main ash place, 16. CO of adding
2Inlet pipe, 17. vapour pipes.
Embodiment
One, installation site, annexation
The utility model filling-up pot 1 is top cylinder shape, lower taper; Diffuser 2 is installed on filling-up pot 1 top and filling-up pot UNICOM; Last manhole 3 is positioned at the top of filling-up pot; Jar in ladder 4 be positioned at manhole 3 below, weld together with the filling-up pot inwall; Last grid distributor 7 is positioned at the centre of round shape; Juice outlet groove 8 is positioned at the outside of filling-up pot, and the bottom communicates with the filling-up pot conical lower portion, goes up to link to each other with full charge juice outlet pipe; Cloth annular groove 5 is welded on the filling-up pot inwall between last grid distributor 7 and filling-up pot inwall; Full charge juice juice opening 6 is positioned at the same level attitude of cloth annular groove 5, is connected in the outside of filling-up pot; Following grid distributor 9 is positioned at columnar bottom, and two connects the filling-up pot inwall, and top connects CO
2Inlet pipe, following grid distributor 9 be one can be movable plate, open the removing lime-ash when being used for shutting down; CO
2Distribution endless tube 10 be positioned at following grid distributor 9 below, have channel-section steel to hold and be welded with the reinforcement steel plate down; Row's end mouth 11 is positioned at the bottom of juice outlet groove 8; Slag removing hole 12 is positioned at the bottom of filling-up pot 1 taper; Following manhole 13 is positioned at columnar surface, closes on taper, the outer wall of external filling-up pot; Predefecation juice entrance 14 is positioned at the mid-way of filling-up pot, tangentially enters into filling-up pot, is level attitude with last grid distributor 7, is connected to the outside of filling-up pot; The master adds the top that ash place 15 is positioned at the predefecation juice pipe; CO
2Gas inlet pipe 16 passes the outer wall of filling-up pot to the middle part, and palintrope welds together with distribution endless tube 10 along to the endless tube 10 that distributes; Vapour pipe 17 is positioned at CO
2The top of gas inlet pipe 16 penetrates in the jar from the outside.
Two, flow process
Among the embodiment shown in the figure, described full charge juice is sugar cane juice or sugar beet juice.Predefecation juice (sugarcane juice) fully mixes the back by cloth annular groove 5 uniform distributions through the main mid-way that tangentially enters into filling-up pot after ash place 15 adds ash that adds.While CO
2Gas is from CO
2Gas enters pipe 16 and enters, and arrives CO
2Distribution endless tube 10, through bubbling up behind the following grid distributor 9, the foam of generation can carry out froth breaking by the steam that vapour pipe 17 enters, CO
2Gas rise with defluent add lye mutually mixed convection current contact; the reverse circulation convection current fully contacts absorption reaction in jar; the gas that produces is by the diffusing gas in diffuser 2 past outsides; the precipitation lime-ash that produces during bubbling; discharge from slag removing hole when waiting to shut down, the full charge juice after the full charge goes out juice through juice outlet groove 8 from full charge juice outlet 6.
Claims (4)
1. a reverse filling-up pot rapidly and efficiently comprises that top is the filling-up pot (1) of round shape, lower taper, is characterized in that: in filling-up pot (1) cylindrical shell CO that from top to bottom enters is housed
2Inlet pipe (16), last grid distributor (7) is located at the centre of full charge device, and following grid distributor (9) is located at the columnar bottom of filling-up pot, and cloth annular groove (5) is located between grid distributor (7) and the full charge device inwall, CO
2Distribution endless tube (10) is located at down under the grid distributor (9), and predefecation juice entrance (14) tangentially enters into filling-up pot from the mid-way of filling-up pot, and the main ash that adds is located the top that (15) are located at the predefecation juice pipe.
2. reverse filling-up pot rapidly and efficiently according to claim 1, it is characterized in that: cloth annular groove (5) is metal cylinder, is welded on filling-up pot (1) inwall, is on the same level attitude with last grid distributor (7).
3. reverse filling-up pot rapidly and efficiently according to claim 1 is characterized in that: the master who is located at predefecation juice pipe top adds ash place (15) and is level attitude with last grid distributor (7), is connected to the outside of filling-up pot.
4. reverse filling-up pot rapidly and efficiently according to claim 1 is characterized in that: CO
2Inlet pipe (16) is passed the outer wall of filling-up pot (1) to the middle part, and palintrope welds together with distribution endless tube (10) along to the endless tube that distributes (10).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220738209 CN203174110U (en) | 2012-12-28 | 2012-12-28 | Fast and efficient reverse carbonating tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220738209 CN203174110U (en) | 2012-12-28 | 2012-12-28 | Fast and efficient reverse carbonating tank |
Publications (1)
Publication Number | Publication Date |
---|---|
CN203174110U true CN203174110U (en) | 2013-09-04 |
Family
ID=49070841
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 201220738209 Expired - Fee Related CN203174110U (en) | 2012-12-28 | 2012-12-28 | Fast and efficient reverse carbonating tank |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN203174110U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106110836A (en) * | 2016-07-04 | 2016-11-16 | 广西大新县雷平永鑫糖业有限公司 | A kind of cane sugar factory carbon-absorbing tower |
CN106139858A (en) * | 2016-07-04 | 2016-11-23 | 广西大新县雷平永鑫糖业有限公司 | A kind of High-efficiency carbon-absorbing tower |
-
2012
- 2012-12-28 CN CN 201220738209 patent/CN203174110U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106110836A (en) * | 2016-07-04 | 2016-11-16 | 广西大新县雷平永鑫糖业有限公司 | A kind of cane sugar factory carbon-absorbing tower |
CN106139858A (en) * | 2016-07-04 | 2016-11-23 | 广西大新县雷平永鑫糖业有限公司 | A kind of High-efficiency carbon-absorbing tower |
CN106110836B (en) * | 2016-07-04 | 2018-06-01 | 广西大新县雷平永鑫糖业有限公司 | A kind of cane sugar factory carbon-absorbing tower |
CN106139858B (en) * | 2016-07-04 | 2018-10-16 | 广西大新县雷平永鑫糖业有限公司 | A kind of High-efficiency carbon-absorbing tower |
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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 |
Granted publication date: 20130904 Termination date: 20151228 |
|
EXPY | Termination of patent right or utility model |