CN203598671U - Multi-tube type adsorption tower - Google Patents
Multi-tube type adsorption tower Download PDFInfo
- Publication number
- CN203598671U CN203598671U CN201320585067.7U CN201320585067U CN203598671U CN 203598671 U CN203598671 U CN 203598671U CN 201320585067 U CN201320585067 U CN 201320585067U CN 203598671 U CN203598671 U CN 203598671U
- Authority
- CN
- China
- Prior art keywords
- absorption
- cylindrical shell
- tower body
- multitube
- adsorption tower
- 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
Images
Landscapes
- Drying Of Gases (AREA)
Abstract
The utility model relates to a multi-tube type adsorption tower for solving the problem that partial compression air cannot be in fully contact with a drying agent in a pressure vessel barrel type adsorption tower due to large inner diameter of the barrel. The multi-tube type adsorption tower disclosed by the utility model comprises a base and an adsorption barrel body arranged on the base, and is characterized in that the adsorption barrel body is composed of a plurality of single tubes, and two ends of each single tube are connected with gas collecting pockets at the upper end and the lower end by a pore plate respectively. The utilization rate of the drying agent and the drying space is increased, the compression air can be in fully contact with the drying agent, the gas quality is improved, the manufacturing requirement on the vessel is low relatively, the manufacturing cycle is shortened and thus the cost is reduced.
Description
Technical field
The utility model relates to air filtration equipment technology field, especially a kind of multitube absorption tower body.
Background technology
Adsorption tower is the equipment of realizing absorption operation Purge gas or liquid, be widely used in industrial production, its function differs, structure is also varied, if patent publication No. is CN102451596A, disclosed a kind of adsorption tower, comprises ventilation head, spherical crown orifice plate, filters and stop layer, center pressure ring, limit pressure ring and admission line, ventilation head is connected on the admission line of adsorption tower, and limit pressure ring and center pressure ring stop layer by filtration and be fixed on spherical crown orifice plate.If patent announcement number is for a kind of adsorption tower that CN202224030U provides, for the later stage adsorption treatment of Industry Waste tail gas, comprise tower body, the bottom of tower body is provided with into mouth, and the top of tower body is outlet flue; The top of tower body inside is provided with spray head, fixes uniformly seven cone cylinders with same configuration in the inner upper and lower orientation of tower body, and cone cylinder is that the large lower ending opening of upper end open is little; Above each cone cylinder, fix a taper cap, taper cap and cone cylinder interlaced arrangement, and the cone point of taper cap is upward, by the interlaced arrangement of cone cylinder and taper cap, in the time spraying water in top, current form seven grades " waterfall ", and object is the time of contact that has extended flue gas and current.And for traditional gas dryer, adsorption tower is generally double shell form, because cylindrical shell belongs to pressure vessel category, therefore the requirement of the manufacture craft of cylindrical shell is high, long in time limit, and cost is high, and because barrel diameter is excessive, cause Partial shrinkage air fully to contact with drier.
Summary of the invention
The purpose of this utility model be for pressure container barrel-type adsorption tower because of cylinder internal diameter large, the problem that causes Partial shrinkage air fully to contact with drier, a kind of reasonable in design is provided, adopts segmentation pipe can make the multitube absorption tower body that in pipe, dry agent fully contacts with air.
Above-mentioned technical problem of the present utility model is mainly solved by following technical proposals: a kind of multitube absorption tower body, comprise base, be arranged on the absorption cylindrical shell on base, it is characterized in that described absorption cylindrical shell is made up of some Zhi Danguan, the two ends of some Zhi Danguan are connected with the gas collection bag at upper and lower two ends respectively by orifice plate.The technical program redesigns original absorption cylindrical shell, utilize perforated plate construction, fix single tube, form a pipe group large cylinder by some Zhi Danguan, two ends are carried out compressed air by gas collection bag and are converged, the drier such as the in-built alundum (Al2O3) of single tube, because single tube internal diameter is less, after compressed air enters, internal pressure equilibrium, drier just can fully carry out absorption to the moisture of compressed air the inside.
As preferably, described absorption cylindrical shell is provided with two side by side, and gas collection is wrapped and is provided with Pressure gauge.As individual overall adsorption tower, two absorption cylindrical shells can carry out low-grade fever regeneration heating, the operations such as regeneration gas balance adjustment.Pressure gauge is arranged on gas collection bag, mainly measures output pressure power.
As preferably, described orifice plate is circular, and single tube sealing is fixed in the through hole that orifice plate is provided with.Circular flange formula orifice plate and hemispherical gas collection package integrator, have high structural strength, between single tube and orifice plate, adopts removable seal to be connected, the convenient drier of in use changing.
As preferably, described adsorption tower air inlet is from the lower end access of absorption cylindrical shell, and air inlet enters absorption cylindrical shell through pneumatic operated valve.Compressed air flows from bottom to top and is adsorbed through absorption cylindrical shell, dry after from upper discharge.
As preferably, two described absorption cylindrical shell upper ends are connected with gas outlet by check valve respectively.Compressed air is after drying as finished product gas, and directly output is used, and check valve prevents from flowing backwards.
As preferably, between two described absorption cylindrical shells, be provided with switch board.Equipment as a whole, makes full use of space, and control operation is also convenient.
Effective effect of the present utility model is: improved the utilization rate of drier and dry place, compressed air obtains fully contacting with drier, has improved GAS QUALITY, the manufacture of container is required relatively low, shorten the manufacturing cycle, thereby reduce costs.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of the present utility model.
Fig. 2 is the right TV structure schematic diagram of the utility model Fig. 1.
In figure: 1. absorption cylindrical shell, 2. switch board, 3. base, 4. Pressure gauge, 5. orifice plate, 6. pneumatic operated valve, 7. air inlet, 8. gas outlet, 9. gas collection bag.
The specific embodiment
Below by embodiment, and by reference to the accompanying drawings, the technical solution of the utility model is described in further detail.
Referring to Fig. 1, Fig. 2, a kind of multitube absorption tower body of the present embodiment, be provided with base 3, two vertical absorption cylindrical shells 1 arranged side by side are installed on base, each absorption cylindrical shell 1 forms by 9 single tubes, and the two ends up and down of single tube are gas collection bags 9, and circular flange formula orifice plate 5 is established in gas collection bag bottom, through hole on orifice plate 5 adopts and snaps in rotary connection with single tube, and is provided with sealing ring.
The upper-part centralized gas bag 9 of two absorption cylindrical shells is equipped with Pressure gauge 4, and the upper end that bottom air inlet 7 is connected into 9, two absorption cylindrical shells 1 of gas collection bag through pneumatic operated valve 6 is connected with gas outlet 8 by check valve respectively.
When work, humid air is entered by air inlet 7, enters absorption cylindrical shell 1 through pneumatic operated valve 6, flows by after the abundant adsorption dry of each single tube from bottom to top, is discharged by gas outlet 8 through check valve.
Above-described embodiment is to explanation of the present utility model, is not to restriction of the present utility model, any structure after simple transformation of the present utility model is all belonged to protection domain of the present utility model.
Claims (6)
1. a multitube absorption tower body, comprise base (3), be arranged on the absorption cylindrical shell (1) on base, it is characterized in that described absorption cylindrical shell (1) is made up of some Zhi Danguan, the two ends of some Zhi Danguan are connected with the gas collection bag (9) at upper and lower two ends respectively by orifice plate (5).
2. a kind of multitube absorption tower body according to claim 1, is characterized in that described absorption cylindrical shell (1) is provided with two side by side, and gas collection bag (9) is provided with Pressure gauge (4).
3. a kind of multitube absorption tower body according to claim 1, is characterized in that described orifice plate (5) is for circular, and single tube sealing is fixed in the through hole that orifice plate is provided with.
4. a kind of multitube absorption tower body according to claim 1 and 2, is characterized in that the lower end access of adsorption tower air inlet (7) from absorption cylindrical shell (1), and air inlet enters absorption cylindrical shell through pneumatic operated valve (6).
5. according to a kind of multitube absorption tower body described in claim 2 or 3, it is characterized in that two described absorption cylindrical shell (1) upper ends are connected with gas outlet (8) by check valve respectively.
6. according to a kind of multitube absorption tower body described in claim 2 or 3, it is characterized in that, between described two absorption cylindrical shells (1), be provided with switch board (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320585067.7U CN203598671U (en) | 2013-09-23 | 2013-09-23 | Multi-tube type adsorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320585067.7U CN203598671U (en) | 2013-09-23 | 2013-09-23 | Multi-tube type adsorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203598671U true CN203598671U (en) | 2014-05-21 |
Family
ID=50711372
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320585067.7U Expired - Fee Related CN203598671U (en) | 2013-09-23 | 2013-09-23 | Multi-tube type adsorption tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203598671U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107719980A (en) * | 2017-11-13 | 2018-02-23 | 国网技术学院 | A kind of storing unit for special operation screening clothing |
-
2013
- 2013-09-23 CN CN201320585067.7U patent/CN203598671U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107719980A (en) * | 2017-11-13 | 2018-02-23 | 国网技术学院 | A kind of storing unit for special operation screening clothing |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201776062U (en) | Inlet gas diffusion device of adsorption tower | |
| CN207886932U (en) | A kind of oxygenerator drying adsorption tower | |
| CN201632181U (en) | PSA gas flow multi-stage diffusing device | |
| CN207928959U (en) | A kind of circulated sprinkling tail gas absorber | |
| CN202185251U (en) | Cylinder structure for absorption tower | |
| CN203598671U (en) | Multi-tube type adsorption tower | |
| CN201164784Y (en) | Heatless regenerative type air-drying machine | |
| CN201823438U (en) | Automatic stepping-down alarm pressing device | |
| CN102139179A (en) | Adjustable gas-liquid separator | |
| CN104728894B (en) | Inertial separation and automatic collection lampblack purifying system | |
| CN205182467U (en) | Novel high -efficient adsorber of gaseous phase mercury | |
| CN204275741U (en) | Venturi umbrella-type spray desulfurization precipitator | |
| CN209549090U (en) | A kind of new and effective activated carbon adsorption device | |
| CN201664567U (en) | Efficient active carbon filter | |
| CN209333460U (en) | A kind of double tower switching air purifier of novel compositions valve | |
| CN104667703B (en) | The combined system of sulfur dioxide in a kind of charcoal absorption stack gases | |
| CN203200021U (en) | Four-tube oxygen making machine | |
| CN208878217U (en) | A kind of medical oxygen producing purifying plant | |
| CN209549430U (en) | Reaction kettle high pressure gas filtering recovering device | |
| CN204746040U (en) | Horizontal compression heat drying equipment of single tower | |
| CN201776032U (en) | Adjustable gas-liquid separator | |
| CN201701863U (en) | Natural gas drying and filtering device | |
| CN205953519U (en) | Pressure swing adsorption nitrogen production equipment's closing device | |
| CN201664569U (en) | PSA whirlwind umbrella type honeycomb airflow diffusing device | |
| CN206152588U (en) | Compressor dry gas bottle |
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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140521 Termination date: 20160923 |