CN201572594U - Adsorption tower - Google Patents
Adsorption tower Download PDFInfo
- Publication number
- CN201572594U CN201572594U CN2010200222305U CN201020022230U CN201572594U CN 201572594 U CN201572594 U CN 201572594U CN 2010200222305 U CN2010200222305 U CN 2010200222305U CN 201020022230 U CN201020022230 U CN 201020022230U CN 201572594 U CN201572594 U CN 201572594U
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- CN
- China
- Prior art keywords
- adsorption tower
- gas
- pipe
- urceolus
- connecting pipe
- 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
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- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model discloses an adsorption tower, which comprises an outer drum (1), a feeding pipe (4), a sealing companion flange (7), support legs (9), a suspension lug (11), an inner drum (12), a connecting pipe (15), a gas outlet pipe (17), a gas inlet pipe (18) and a companion flange (21). The connecting pipe (15) connects the outer drum (1) with the inner drum (12), gas enters from the inner drum (12) and exits from the outer drum (1), air outlets are uniformly distributed on a portion, inside the outer drum (1), of the connecting pipe (15), and the gas inlet pipe (18) is sleeved inside the connecting pipe (15). The adsorption tower lengthens flow path of the gas inside the adsorption tower, increases raw material adsorption rate, and resolves the problems of low adsorption rate, poor produced gas quality and the like in the prior art.
Description
Technical field
The utility model relates to a kind of adsorption tower, relates in particular to a kind of gas apparatus adsorption tower.
Background technology
In China, the development of industrial gasses equipment has been widely used in industries such as metallurgy, petrochemical industry, chemical fertilizer, urban coal gasification, machinery, electronics, glass, chemical fibre rapidly.
Yet in the process of gas apparatus aerogenesis, flow path is short during Primordial Qi absorption, the aerogenesis quality of adsorption tower is low, thereby influence the aerogenesis of gas apparatus, the primary stage of making, what adopt is the straight barrel type absorber, this structure is easy to process, but in the process of aerogenesis, require absorber to have ratio of height to diameter, extraordinary shipborne equipment ratio of height to diameter abortion gas is of poor quality, have to increase adsorption tower and prolong the path, we press for and design a kind of suitable absorber, solve problems such as the raw material adsorption efficiency is low, aerogenesis is of poor quality.
The utility model content
Problems such as the purpose of this utility model is to provide a kind of adsorption tower, and is low with the raw material adsorption efficiency that solves absorber of the prior art, that aerogenesis is of poor quality.
For achieving the above object, the technical solution adopted in the utility model is: described adsorption tower mainly comprises urceolus, charge pipe, sealing companion flange, supporting leg, hanger, inner core, tube connector, escape pipe, air inlet pipe and companion flange, tube connector connects urceolus and inner core, gas is advanced by inner core, urceolus goes out, the part of tube connector in urceolus has equally distributed venthole, and air inlet pipe is enclosed within tube connector inside.
Compare with prior art, the utlity model has following advantage:
Prolong the path that flows to of gas, reduced the quantity of adsorption tower, improved the adsorption rate and the aerogenesis quality of raw material.
Description of drawings
Fig. 1 is a cutaway view of the present utility model;
Fig. 2 is an axonometric drawing of the present utility model.
Among the figure
1 urceolus, 4 charge pipes, 7 sealing companion flanges, 9 supporting legs, 11 hangers
12 inner cores, 15 tube connectors, 17 escape pipes, 18 air inlet pipe, 21 companion flanges
The specific embodiment
Below in conjunction with accompanying drawing, specify the utility model.
The utility model mainly comprises urceolus 1, charge pipe 4, sealing companion flange 7, supporting leg 9, hanger 11, inner core 12, tube connector 15, escape pipe 17, air inlet pipe 18 and companion flange 21, urceolus 1 links together with inner core 12 usefulness tube connectors 15, gas is advanced by inner core 12, urceolus 1 goes out, tube connector 15 connects urceolus 1 and inner core 12, the part of tube connector 15 in urceolus 1 has equally distributed venthole, air inlet pipe 18 is enclosed within tube connector 15 inside, according to the pressure pipeline design standard, the pneumatics principle, the gas motion theory, prolonged gas flow path in the adsorption tower, improved the raw material adsorption rate, it is low to have solved in the prior art raw material adsorption efficiency, problems such as aerogenesis is of poor quality.
More than disclosed be the specific embodiment of this patent only, but this patent is not limited thereto, any those skilled in the art can think variation, all should drop in the protection domain of this patent.
Claims (2)
1. adsorption tower, it is characterized in that: it mainly comprises urceolus (1), charge pipe (4), sealing companion flange (7), supporting leg (9), hanger (11), inner core (12), tube connector (15), escape pipe (17), air inlet pipe (18) and companion flange (21), tube connector (15) connects urceolus (1) and inner core (12), gas is advanced by inner core (12), and urceolus (1) goes out.
2. a kind of adsorption tower according to claim 1 is characterized in that: the part of described tube connector (15) in urceolus (1) has equally distributed venthole, and air inlet pipe (18) is enclosed within tube connector (15) inside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010200222305U CN201572594U (en) | 2010-01-18 | 2010-01-18 | Adsorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010200222305U CN201572594U (en) | 2010-01-18 | 2010-01-18 | Adsorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201572594U true CN201572594U (en) | 2010-09-08 |
Family
ID=42692473
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010200222305U Expired - Fee Related CN201572594U (en) | 2010-01-18 | 2010-01-18 | Adsorption tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201572594U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107138045A (en) * | 2017-06-12 | 2017-09-08 | 青岛双瑞海洋环境工程股份有限公司 | Marine exhaust processing unit for removing sulfur and nitrogen oxides simultaneously |
| CN108219828A (en) * | 2018-02-05 | 2018-06-29 | 山东星火科学技术研究院 | A kind of desulfurization adsorption tower |
-
2010
- 2010-01-18 CN CN2010200222305U patent/CN201572594U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107138045A (en) * | 2017-06-12 | 2017-09-08 | 青岛双瑞海洋环境工程股份有限公司 | Marine exhaust processing unit for removing sulfur and nitrogen oxides simultaneously |
| CN108219828A (en) * | 2018-02-05 | 2018-06-29 | 山东星火科学技术研究院 | A kind of desulfurization adsorption 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100908 Termination date: 20130118 |