CN203540129U - Coal chemical separating column - Google Patents
Coal chemical separating column Download PDFInfo
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- CN203540129U CN203540129U CN201320679775.7U CN201320679775U CN203540129U CN 203540129 U CN203540129 U CN 203540129U CN 201320679775 U CN201320679775 U CN 201320679775U CN 203540129 U CN203540129 U CN 203540129U
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- coal chemical
- plate structure
- tower
- chemical industry
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Abstract
The utility model discloses a coal chemical separating column. The coal chemical separating column comprises a reaction separation region and a material collecting region, wherein a plurality of support ring structures are arranged in different heights on the inner wall of the reaction separation region, a column plate structure is obliquely arranged between two support rings, the column plate structure inclines with 60 degrees horizontally, a packing layer formed by packing is arranged in a gap between the column plate structure and the inner wall, and a plurality of vertical sieve pore structures are arranged on the column plate structure. The coal chemical separating column has simple structure, has good separation effect on coal chemical liquid raw material by virtue of the structures of the oblique column plate and the packing layers, the contact area of the liquid raw material and the packing is increased, the wall flowing effect is avoided, the production cost of enterprises is reduced, and the working efficiency of enterprises is improved.
Description
Technical field
The utility model relates to Coal Chemical Industry separation equipment field, relates in particular to the knockout tower of processing in a kind of Coal Chemical Industry reaction.
Background technology
Coal Chemical Industry refers to take coal as raw material, through chemical process, makes coal be converted into the process of gas, liquid and solid fuel and chemicals.Mainly comprise coal gasification, liquefaction, destructive distillation, and tar processing and carbide acetylene chemical industry, liquid fuel or chemicals that reaction generates mix, and are difficult to be isolated out, and therefore by knockout tower, pass through extract and separate effect and different fuel or chemicals can be separated.
Common knockout tower is vertical column plate and packing layer structure, liquid charging stock is entering into packing layer, due to the sidewall smoother of tower body, liquid charging stock flows with easily forming wall on sidewall, cause separating effect variation, affect the quality of product, and, liquid charging stock is because Action of Gravity Field is vertically dirty in packing layer, liquid charging stock and packing layer are shorter time of contact, separating effect is relatively poor, common method improves separating effect by the length of adding packing layer, cause like this recruitment cost of knockout tower greatly to increase, improved the production cost of enterprise.
Utility model content
For the problem of above-mentioned existence, the knockout tower that provides a kind of Coal Chemical Industry simple in structure, good separating effect to apply is provided the utility model object.
In order to achieve the above object, the technical solution adopted in the utility model is as follows: a kind of Coal Chemical Industry knockout tower, described knockout tower comprises Reaction Separation district and material collection district, the differing heights of the inwall in described Reaction Separation district is provided with multiple support ring structures, between two described support rings, be tiltedly installed with tower plate structure, the horizontal tilt angle of described tower plate structure is 60 °, in the interstice coverage of the formation between described two tower plate structures and inwall, be provided with filler and form packing layer, described tower plate structure is provided with multiple vertical screen pore structures.
Liquid charging stock is when through column plate and packing layer, and because column plate is for tilting to install, due to Action of Gravity Field, liquid charging stock can progressively enter the packing layer of lower floor by vertical screen pore structure, and shunting effective guaranteed fully contacting of liquid charging stock and packing layer; Meanwhile, liquid charging stock is in the vertical dirty process of packing layer, and when it arrives the tower plate structure of lower floor, further shunting, has improved the separating effect of packing area.
As a kind of improvement of the present utility model; the top in described Reaction Separation district is provided with raw material intake line and protective gas intake line; the top of described raw material intake line is provided with multiple showerhead configuration; raw material is input to Reaction Separation district by showerhead configuration; short grained liquid convenience fully contacts with filler; protective gas intake line is applicable to the separation of variety classes liquid charging stock simultaneously, and usage range is wide.
As a kind of improvement of the present utility model, the sidewall of described packing layer is provided with filler clean-up port, by filler clean-up port is convenient, clears up in time and changes filler, simple to operation.
As a kind of improvement of the present utility model, described collecting region bottom is provided with material collection mouth, sieve plate and discharge of materials mouth, the collection mouth that described material collection mouth is taper, and the below of described cone-shaped collection mouth is provided with flow distribution plate; Liquid charging stock after separation splashes in material collection mouth by Action of Gravity Field, and the collection mouth of taper facilitates the collection of material, simultaneously by the flow velocity of flow distribution plate Structure Decreasing liquid charging stock, and convenient collection.
The utility model has the advantage of: the utility model is simple in structure, by the column plate and the packing layer structure that tilt, the liquid charging stock of Coal Chemical Industry is had to good separating effect, improved the contact area of liquid charging stock and filler, prevent the generation of wall stream effect, reduce the production cost of enterprise, improved the operating efficiency of enterprise.
Accompanying drawing explanation
Fig. 1 is the utility model structure diagram;
Wherein, 1 Reaction Separation district, 2 material collection districts; 3 raw material output pipes, 4 showerhead configuration, 5 protective gas intake lines; 6 support ring structures, 7 tower plate structures, 8 upper strata packing layers; 9 lower floor's packing layers, 10 filler clean-up ports, 11 vertical screen pore structures; 12 material collection mouths; 13 flow distribution plates, 14 sieve plates, 15 discharge of materials mouths.
The specific embodiment
Below in conjunction with accompanying drawing explanation and the specific embodiment, the utility model is described in further detail.
embodiment 1:a kind of Coal Chemical Industry knockout tower as shown in Figure 1, described knockout tower comprises Reaction Separation district 1 and material collection district 2, the differing heights of the inwall in described Reaction Separation district 1 is provided with multiple support ring structures 6, between two described support rings, be tiltedly installed with tower plate structure 7, the horizontal tilt angle of described tower plate structure 7 is 60 °, in the interstice coverage of the formation between described two tower plate structures and inwall, be provided with filler and form packing layer 8 and 9, described tower plate structure 7 is provided with multiple vertical screen pore structures 11.
Liquid charging stock is when through column plate 7 and upper strata packing layer 8, because column plate 7 is for tilting to install, due to Action of Gravity Field, liquid charging stock can progressively enter the packing layer 9 of lower floor by vertical sieve aperture 11 structures, shunting effective, has guaranteed fully contacting of liquid charging stock and packing layer; Meanwhile, liquid charging stock is in the vertical dirty process of packing layer, and when it arrives the tower plate structure of lower floor, further shunting, has improved the separating effect of packing area.
embodiment 2:as shown in Figure 1; the top in described Reaction Separation district 1 is provided with raw material intake line 3 and protective gas intake line 5; the top of described raw material intake line 3 is provided with multiple showerhead configuration 4; raw material is input to Reaction Separation district 1 by showerhead configuration 4; short grained liquid convenience fully contacts with filler; protective gas intake line 5 is applicable to different types of liquid charging stock separation simultaneously, and usage range is wide.
embodiment 3:as shown in Figure 1, the sidewall of described packing layer 8 and 9 is provided with filler clean-up port 10, by the convenient cleaning in time in filler clean-up port 10 and replacing filler, simple to operation.
embodiment 4:as shown in Figure 1, described collecting region bottom is provided with material collection mouth 12, sieve plate 14 and discharge of materials mouth 15, the collection mouth that described material collection mouth 12 is taper, and the below of described cone-shaped collection mouth 12 is provided with flow distribution plate 13; Liquid charging stock after separation splashes in material collection mouth 12 by Action of Gravity Field, and the collection mouth 12 of taper facilitates the collection of material, reduces the flow velocity of liquid charging stock by flow distribution plate structure 13 simultaneously, convenient collection.
It should be noted that, above-mentioned is only preferred embodiment of the present utility model, is not used for limiting protection domain of the present utility model, and the equivalents of having done on the basis of above-described embodiment all belongs to protection domain of the present utility model.
Claims (4)
1. a Coal Chemical Industry knockout tower, described knockout tower comprises Reaction Separation district and material collection district, it is characterized in that, the differing heights of the inwall in described Reaction Separation district is provided with multiple support ring structures, between two described support rings, be tiltedly installed with tower plate structure, the horizontal tilt angle of described tower plate structure is 60 °, is provided with filler and forms packing layer in the interstice coverage of the formation between described two tower plate structures and inwall, and described tower plate structure is provided with multiple vertical screen pore structures.
2. Coal Chemical Industry knockout tower according to claim 1, is characterized in that, the top in described Reaction Separation district is provided with raw material intake line and protective gas intake line, and the top of described raw material intake line is provided with multiple showerhead configuration.
3. Coal Chemical Industry knockout tower according to claim 1, is characterized in that, the sidewall of described packing layer is provided with filler clean-up port.
4. Coal Chemical Industry knockout tower according to claim 1, is characterized in that, described collecting region bottom is provided with material collection mouth, sieve plate and discharge of materials mouth, the collection mouth that described material collection mouth is taper, and the below of described cone-shaped collection mouth is provided with flow distribution plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320679775.7U CN203540129U (en) | 2013-10-31 | 2013-10-31 | Coal chemical separating column |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320679775.7U CN203540129U (en) | 2013-10-31 | 2013-10-31 | Coal chemical separating column |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203540129U true CN203540129U (en) | 2014-04-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320679775.7U Expired - Fee Related CN203540129U (en) | 2013-10-31 | 2013-10-31 | Coal chemical separating column |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203540129U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106178747A (en) * | 2016-08-20 | 2016-12-07 | 浙江众立机械制造有限公司 | Cleaner |
-
2013
- 2013-10-31 CN CN201320679775.7U patent/CN203540129U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106178747A (en) * | 2016-08-20 | 2016-12-07 | 浙江众立机械制造有限公司 | Cleaner |
| CN106178747B (en) * | 2016-08-20 | 2018-11-06 | 浙江众立机械制造有限公司 | Cleaner |
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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: 20140416 Termination date: 20141031 |
|
| EXPY | Termination of patent right or utility model |