CN202921023U - Adsorbing-decolorizing-refining tower for active carbon - Google Patents
Adsorbing-decolorizing-refining tower for active carbon Download PDFInfo
- Publication number
- CN202921023U CN202921023U CN 201220538018 CN201220538018U CN202921023U CN 202921023 U CN202921023 U CN 202921023U CN 201220538018 CN201220538018 CN 201220538018 CN 201220538018 U CN201220538018 U CN 201220538018U CN 202921023 U CN202921023 U CN 202921023U
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- CN
- China
- Prior art keywords
- decolorizing
- tower
- bleaching tower
- storage tank
- active carbon
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- 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
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- Treatment Of Liquids With Adsorbents In General (AREA)
Abstract
The utility model discloses an adsorbing-decolorizing-refining tower for active carbon. The adsorbing-decolorizing-refining tower comprises a material storage tank and a decolorizing tower, wherein a charging hole is formed in the top end of the material storage tank; a material conveying port is formed in the bottom end of the material storage tank; the material conveying port is communicated with the charging hole in one side of the top of the decolorizing tower by a material conveying pipeline; a pipeline filter is arranged on the material conveying pipeline; the material storage tank is arranged on a plane higher than the charging hole in the top of the decolorizing tower; a decolorizing barrel is arranged between two walls inside the decolorizing tower; a plurality of decolorizing layers are in parallel arranged inside the decolorizing barrel from the top to the bottom; the decolorizing layers are of net rack structures which are not provided with covers at the upper ends and of grid types at the lower ends; and an active carbon filler is placed inside the decolorizing layers; and a discharging hole is formed in the bottom of the discoloring tower. The adsorbing-decolorizing-refining tower has the beneficial effects of being novel in structure and simple and convenient to operate, the energy consumption is effectively reduced, the service life of the active carbon for decolorizing is prolonged, the waste of resources is reduced, and a decolorizing effect is improved.
Description
(1) technical field
It is a kind of thick along sour decolorizing and refining equipment that the utility model belongs to, and particularly relates to a kind of charcoal absorption decolorizing and refining tower.
(2) background technology
At present, thick decolouring step along chemical products such as acid all will use enamel still mostly, will active carbon and slightly complete decolorization through filtering after dropping into the enamel still stirring and dissolving along acid sludge is common.Yet this method is easy to make active carbon broken, causes most of active carbon once to use, and very waste simultaneously will be thick during along acid and active carbon stirring and dissolving with enamel still, stir and heating need to power larger, decolorizing effect is also unstable.Therefore, be necessary to make that a kind of energy consumption is low, the repeatedly used decolorizing and refining tower of active carbon, reduce the waste of resource, promote decolorizing effect.
(3) utility model content
In order to overcome existing thick weak point along sour decolorizing and refining equipment, the utility model provides a kind of charcoal absorption decolorizing and refining tower.
The technical solution of the utility model is to realize like this.
A kind of charcoal absorption decolorizing and refining tower of this programme, comprise storage tank and bleaching tower, described storage tank top is provided with charging aperture, described storage tank bottom is provided with conveying mouth, this conveying mouth is communicated with by feeding pipe with the feeding mouth that is arranged on bleaching tower top one side, is provided with piping filter on this feeding pipe; Described storage tank is arranged on plane higher than bleaching tower top feeding mouth; Be provided with the decolouring cylinder between inner two walls of described bleaching tower, this decolouring inside is arranged with several decoloring layers from the top in parallel on bottom direction, described some decoloring layers are the grid structure of upper end uncovered, lower end grid type, and inside all is placed with active carbon filler; Described bleaching tower bottom is provided with discharging opening.
Described bleaching tower is provided with three, is divided into the first bleaching tower, the second bleaching tower and the 3rd bleaching tower; The discharging opening of described the first bleaching tower is communicated with by pipeline (10) with the feeding mouth of the second bleaching tower, and the feeding mouth of the discharging opening of the second bleaching tower and the 3rd bleaching tower passes through pipeline communication.
Usefulness of the present utility model is: this decolorizing and refining tower structure is novel, and is easy and simple to handle, effectively reduced energy consumption, extended the service life of the active carbon of decolouring use, promoted decolorizing effect when having reduced the wasting of resources.
(4) description of drawings
Accompanying drawing is institutional framework schematic diagram of the present utility model.
(5) specific embodiment
Below in conjunction with embodiment, the specific embodiment of the present utility model is made brief description.
A kind of charcoal absorption decolorizing and refining tower as figure, comprise storage tank 1 and bleaching tower 2, described storage tank 1 top is provided with charging aperture 3, described storage tank 1 bottom is provided with conveying mouth 4, this conveying mouth 4 is communicated with by feeding pipe with the feeding mouth 6 that is arranged on bleaching tower 2 top one sides, is provided with piping filter 5 on this feeding pipe; Described storage tank 1 is arranged on plane higher than bleaching tower 2 top feeding mouths 6; Be provided with decolouring cylinder 7 between inner two walls of described bleaching tower 2, this decolouring 7 inside are arranged with several decoloring layers 8 from the top in parallel on bottom direction, described some decoloring layers 8 are the grid structure of upper end uncovered, lower end grid type, and inside all is placed with active carbon filler; Described bleaching tower 2 bottoms are provided with discharging opening 9.
Described bleaching tower 2 is provided with three, is divided into the first bleaching tower, the second bleaching tower and the 3rd bleaching tower; The discharging opening of described the first bleaching tower is communicated with by pipeline 10 with the feeding mouth of the second bleaching tower, and the feeding mouth of the discharging opening of the second bleaching tower and the 3rd bleaching tower passes through pipeline communication.
The course of work of this example: when using this decolorizing and refining tower to carry out thick suitable acid decolouring step, first pour water and thick suitable acid sludge into storage tank 1 inner dissolving by charging aperture 3, then the thick suitable aqueous acid after dissolving passes through feeding pipe by conveying mouth 4, enter bleaching tower 2 inside from feeding mouth 6, process piping filter 5 when thick suitable aqueous acid flows in feeding pipe, undissolved thick suitable sour solid particle can be filtered out, guaranteeing to enter bleaching tower 2 complete is thick suitable aqueous acid liquid.after thick suitable aqueous acid liquid enters bleaching tower 2 by feeding mouth 6, carry out bleaching process by decolouring cylinder 7, when thick when entering decolouring cylinder 7 along aqueous acid, pass through successively some decoloring layers 8, this moment, decoloring layer 8 inner active carbon fillers of filling can absorb along the pigment impurity in aqueous acid thick, complete the decolouring step, in order to strengthen decolorizing effect, be provided with three bleaching towers 2, be respectively the first bleaching tower, the second bleaching tower and the 3rd bleaching tower, and the discharging opening of the first bleaching tower is communicated with by pipeline 10 with the feeding mouth of the second bleaching tower, the feeding mouth of the discharging opening of the second bleaching tower and the 3rd bleaching tower passes through pipeline communication, three bleaching towers 2 are connected in series together, can repeatedly decolour along aqueous acid thick like this, reach more perfect decolorizing effect, after completing the decolouring step, the thick discharge from the discharging opening 9 of last bleaching tower 2 along aqueous acid carried out subsequent handling.
Above an embodiment of the present utility model is had been described in detail, but described content is only preferred embodiment of the present utility model, can not be considered to be used to limiting practical range of the present utility model.All equalizations of doing according to the utility model application range change and improve etc., within all should still belonging to patent covering scope of the present utility model.
Claims (2)
1. charcoal absorption decolorizing and refining tower, comprise storage tank (1) and bleaching tower (2), it is characterized in that: described storage tank (1) top is provided with charging aperture (3), described storage tank (1) bottom is provided with conveying mouth (4), this conveying mouth (4) is communicated with by feeding pipe with the feeding mouth (6) that is arranged on bleaching tower (2) top one side, is provided with piping filter (5) on this feeding pipe; Described storage tank (1) is arranged on plane higher than bleaching tower (2) top feeding mouth (6); Be provided with decolouring cylinder (7) between inner two walls of described bleaching tower (2), this decolouring cylinder (7) is inner is arranged with several decoloring layers (8) from the top in parallel on bottom direction, described some decoloring layers (8) are the grid structure of upper end uncovered, lower end grid type, and inside all is placed with active carbon filler; Described bleaching tower (2) bottom is provided with discharging opening (9).
2. a kind of charcoal absorption decolorizing and refining tower according to claim 1, it is characterized in that: described bleaching tower (2) is provided with three, is divided into the first bleaching tower, the second bleaching tower and the 3rd bleaching tower; The discharging opening of described the first bleaching tower is communicated with by pipeline (10) with the feeding mouth of the second bleaching tower, and the feeding mouth of the discharging opening of the second bleaching tower and the 3rd bleaching tower passes through pipeline communication.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220538018 CN202921023U (en) | 2012-10-19 | 2012-10-19 | Adsorbing-decolorizing-refining tower for active carbon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220538018 CN202921023U (en) | 2012-10-19 | 2012-10-19 | Adsorbing-decolorizing-refining tower for active carbon |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202921023U true CN202921023U (en) | 2013-05-08 |
Family
ID=48211016
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220538018 Expired - Fee Related CN202921023U (en) | 2012-10-19 | 2012-10-19 | Adsorbing-decolorizing-refining tower for active carbon |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202921023U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105237497A (en) * | 2015-09-21 | 2016-01-13 | 丹阳市助剂化工厂有限公司 | Decolorizeng tank for epoxidized soybean oil production |
| CN105238559A (en) * | 2015-09-21 | 2016-01-13 | 丹阳市助剂化工厂有限公司 | Secondary comprehensive decolorizing tank for epoxidized soybean oil production |
| CN105254593A (en) * | 2015-09-21 | 2016-01-20 | 丹阳市助剂化工厂有限公司 | Two-stage efficient comprehensive decolorizing tank for epoxidized soybean oil production |
| CN107364919A (en) * | 2017-07-28 | 2017-11-21 | 毛旭 | It is a kind of be used to decolourizing, the wastewater treatment composition of taste removal and precipitation |
| CN114470868A (en) * | 2022-02-22 | 2022-05-13 | 瑞昌市渝瑞实业有限公司 | Method and system for separating allantoin from yam mucus and method for preparing skin lotion |
| CN115925659A (en) * | 2022-12-13 | 2023-04-07 | 新疆至臻化工工程研究中心有限公司 | Method for pretreating maleic anhydride absorption liquid |
-
2012
- 2012-10-19 CN CN 201220538018 patent/CN202921023U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105237497A (en) * | 2015-09-21 | 2016-01-13 | 丹阳市助剂化工厂有限公司 | Decolorizeng tank for epoxidized soybean oil production |
| CN105238559A (en) * | 2015-09-21 | 2016-01-13 | 丹阳市助剂化工厂有限公司 | Secondary comprehensive decolorizing tank for epoxidized soybean oil production |
| CN105254593A (en) * | 2015-09-21 | 2016-01-20 | 丹阳市助剂化工厂有限公司 | Two-stage efficient comprehensive decolorizing tank for epoxidized soybean oil production |
| CN105254593B (en) * | 2015-09-21 | 2018-03-30 | 丹阳市助剂化工厂有限公司 | Epoxidized soybean oil production efficiently integrates bleacher with two level |
| CN105237497B (en) * | 2015-09-21 | 2018-04-24 | 丹阳市助剂化工厂有限公司 | Epoxidized soybean oil production bleacher |
| CN105238559B (en) * | 2015-09-21 | 2019-06-14 | 丹阳市助剂化工厂有限公司 | The epoxidized soybean oil production comprehensive bleacher of second level |
| CN107364919A (en) * | 2017-07-28 | 2017-11-21 | 毛旭 | It is a kind of be used to decolourizing, the wastewater treatment composition of taste removal and precipitation |
| CN114470868A (en) * | 2022-02-22 | 2022-05-13 | 瑞昌市渝瑞实业有限公司 | Method and system for separating allantoin from yam mucus and method for preparing skin lotion |
| CN115925659A (en) * | 2022-12-13 | 2023-04-07 | 新疆至臻化工工程研究中心有限公司 | Method for pretreating maleic anhydride absorption liquid |
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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: 20130508 Termination date: 20141019 |
|
| EXPY | Termination of patent right or utility model |