CN215250664U - Multifunctional integrated tower for blast furnace gas - Google Patents
Multifunctional integrated tower for blast furnace gas Download PDFInfo
- Publication number
- CN215250664U CN215250664U CN202121173064.3U CN202121173064U CN215250664U CN 215250664 U CN215250664 U CN 215250664U CN 202121173064 U CN202121173064 U CN 202121173064U CN 215250664 U CN215250664 U CN 215250664U
- Authority
- CN
- China
- Prior art keywords
- tower
- blast furnace
- tower body
- section
- furnace gas
- 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.)
- Active
Links
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a multifunctional integrated blast furnace gas tower. The integrated tower comprises a tower body, and an airflow distribution pipe is arranged at the lower part in the tower body; a dust interception section, a dry dechlorination section and/or a hydrolysis conversion section are/is arranged in the tower body above the airflow distribution pipe. The integrated tower can realize the functions of a plurality of tower bodies by properly increasing the tower diameter and the tower height. The tower body floor area can be effectively reduced, and the equipment investment is reduced.
Description
Technical Field
The utility model relates to a multifunctional integrated tower for blast furnace gas.
Background
The sulfur in blast furnace gas of iron and steel enterprises mainly comprises H2S and COS, wherein H2S accounts for about 30%, and COS accounts for about 70%. H2The removal of S is relatively easy, and the key point and difficulty of the fine desulfurization of blast furnace gas lies in the removal of COS. The removal of COS can adopt an adsorption method or a hydrolysis conversion method, wherein the hydrolysis conversion method is to convert COS into H by a hydrolysis catalyst2S, then H is removed2And S. The blast furnace gas has complex components and contains dust, chloride ions and the like, which influence the service life of the hydrolysis catalyst. Therefore, in industrial applications, facilities such as a pretreatment column are added before the hydrolysis column. The tower body is more, the occupied area is large, and the investment is large.
SUMMERY OF THE UTILITY MODEL
In order to overcome the problems, the utility model aims to provide a multifunctional integrated blast furnace gas tower,
the utility model relates to a blast furnace gas multifunctional integrated tower, which comprises a tower body, wherein the lower part in the tower body is provided with an airflow distribution pipe; a dust interception section, a dry dechlorination section and/or a hydrolysis conversion section are/is arranged in the tower body above the airflow distribution pipe.
Furthermore, the lower part of the airflow distribution pipe is connected with a main pipe of a coal gas inlet, and the upper part of the airflow distribution pipe is provided with a plurality of coal gas branch pipes.
Furthermore, the dry dechlorination section is provided with an upper clapboard and a lower clapboard of a packing layer, the clapboards are composed of a main beam and a secondary beam, and a dry dechlorination agent is filled between the upper clapboard and the lower clapboard.
Furthermore, the hydrolysis conversion section is provided with an upper clapboard and a lower clapboard of a packing layer, the clapboards are composed of a main beam and a secondary beam, and a hydrolysis catalyst is filled between the upper clapboard and the lower clapboard.
Furthermore, a dust and water removing and discharging facility is arranged at the bottom of the tower body.
Furthermore, the ash-removing and water-discharging facility comprises a lower cone at the lower end of the tower body, and a water discharging pipe is arranged at the bottom end of the lower cone; the side end of the lower cone is provided with an ash removing pipe.
Furthermore, the diameter of the tower body of the integrated tower is larger than that of an independent pretreatment tower or hydrolysis tower.
The utility model discloses fall into a plurality of sections with the tower body, a tower body realizes the function of dust interception, dry process dechlorination and the conversion of hydrolysising simultaneously. Because the tower diameter of the integrated tower is slightly increased, in order to ensure that gas airflow uniformly passes through each section of the tower body, the gas inlet pipe is provided with an airflow distribution pipe. This novel multi-functional integrative tower of blast furnace gas can effectively reduce tower body quantity, and then reduces area, reduces the investment.
Drawings
Fig. 1 is a schematic diagram of the present invention.
In the figure, 1 is an airflow distribution pipe, 2 is a dust interception section, 3 is a dry dechlorination section, 4 is a hydrolysis conversion section, and 5 is an ash conveying and draining facility.
The specific implementation mode is as follows:
the invention will be further described with reference to the accompanying drawings and specific embodiments.
The utility model discloses a multi-functional integrative tower of blast furnace gas includes at least: airflow distribution pipe, dust blocking section, dry dechlorinating section, hydrolysis conversion section and ash conveying and draining facility.
Example 1
The tower body diameter of the integrated tower is larger than that of an independent pretreatment tower or hydrolysis tower, and in order to ensure that gas airflow uniformly passes through each section of tower body, the gas inlet pipe is provided with an airflow distribution pipe. The lower part of the airflow distribution pipe is connected with the main pipe of the gas inlet, and the upper part of the airflow distribution pipe is provided with a plurality of gas branch pipes which can evenly distribute the gas. The left end and the right end of the airflow distribution pipe are fixed inside the tower body through flanges. The dust intercepting section is provided with a filter screen and other facilities, intercepted dust is attached to the intercepting device, nitrogen is periodically introduced to purge and clear blockage, and the purge ring is arranged to an external dust-removing groove and other facilities through a dust-removing pipe. The dry dechlorination section is provided with an upper clapboard and a lower clapboard of a packing layer, the clapboard consists of a main beam and a secondary beam, and a dry dechlorination agent is filled between the upper clapboard and the lower clapboard. The hydrolysis conversion section is provided with an upper clapboard and a lower clapboard of a packing layer, the clapboards are composed of a main beam and a secondary beam, and a hydrolysis catalyst is filled between the upper clapboard and the lower clapboard.
The integrated tower can realize the functions of a plurality of tower bodies by properly increasing the tower diameter and the tower height. The tower body floor area can be effectively reduced, and the equipment investment is reduced.
Example 2
The tower body diameter of the integrated tower is larger than that of an independent pretreatment tower or hydrolysis tower, and in order to ensure that gas airflow uniformly passes through each section of tower body, the gas inlet pipe is provided with an airflow distribution pipe. The lower part of the airflow distribution pipe is connected with the main pipe of the gas inlet, and the upper part of the airflow distribution pipe is provided with a plurality of gas branch pipes which can evenly distribute the gas. The left end and the right end of the airflow distribution pipe are fixed inside the tower body through flanges. A first-stage dust interception section, a two-stage dry dechlorination section and a two-stage hydrolysis conversion section are arranged in the tower body from bottom to top;
the bottom of the tower body is provided with a dust-removing and water-discharging facility which comprises a lower cone at the lower end of the tower body, a water discharging pipe arranged at the bottom end of the lower cone and a dust-removing pipe arranged at the side end of the lower cone. The ash conveying pipe is connected to the ash conveying groove, and the water discharging pipe is connected to the water discharging pit.
In the embodiment, the integrated tower can realize the functions of a plurality of tower bodies by properly increasing the tower diameter and the tower height. The tower body floor area can be effectively reduced, and the equipment investment is reduced.
Example 3
As a variation of the above embodiment, different combinations of functional segments are provided in the tower body of the integrated tower of the present embodiment;
the combination is as follows: a two-stage dust interception section and a two-stage dry dechlorination section are arranged in the tower body from bottom to top;
combining two: a two-stage dry dechlorination section and a two-stage hydrolysis conversion section are arranged in the tower body from bottom to top;
combining three components: a two-stage dust interception section, a two-stage dry dechlorination section and a two-stage hydrolysis conversion section are arranged in the tower body from bottom to top;
the above is only a preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any changes or substitutions that can be easily conceived by those skilled in the art within the technical scope of the present invention should be covered by the scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope defined by the claims.
Claims (5)
1. A blast furnace gas multifunctional integrated tower is characterized in that: the integrated tower comprises a tower body, and an airflow distribution pipe is arranged at the lower part in the tower body; a dust interception section, a dry dechlorination section and/or a hydrolysis conversion section are/is arranged in the tower body above the airflow distribution pipe.
2. The blast furnace gas multifunctional integrated tower of claim 1, wherein: the lower part of the airflow distribution pipe is connected with a main pipe of a coal gas inlet, and the upper part of the airflow distribution pipe is provided with a plurality of coal gas branch pipes.
3. The blast furnace gas multifunctional integrated tower of claim 1, wherein: the dry dechlorination section is provided with an upper clapboard and a lower clapboard of a packing layer, the clapboards are composed of a main beam and a secondary beam, and a dry dechlorination agent is filled between the upper clapboard and the lower clapboard.
4. The blast furnace gas multifunctional integrated tower of claim 1, wherein: the hydrolysis conversion section is provided with an upper and a lower clapboards of a packing layer, the clapboards are composed of a main beam and a secondary beam, and a hydrolysis catalyst is filled between the upper and the lower clapboards.
5. The blast furnace gas multifunctional integrated tower of claim 1, wherein: the bottom of the tower body is provided with a dust-removing and water-draining facility.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202121173064.3U CN215250664U (en) | 2021-05-28 | 2021-05-28 | Multifunctional integrated tower for blast furnace gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202121173064.3U CN215250664U (en) | 2021-05-28 | 2021-05-28 | Multifunctional integrated tower for blast furnace gas |
Publications (1)
Publication Number | Publication Date |
---|---|
CN215250664U true CN215250664U (en) | 2021-12-21 |
Family
ID=79474254
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202121173064.3U Active CN215250664U (en) | 2021-05-28 | 2021-05-28 | Multifunctional integrated tower for blast furnace gas |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN215250664U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113388423A (en) * | 2021-05-28 | 2021-09-14 | 中冶华天工程技术有限公司 | Blast furnace gas dust interception, dry dechlorination and hydrolysis conversion integrated tower |
-
2021
- 2021-05-28 CN CN202121173064.3U patent/CN215250664U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113388423A (en) * | 2021-05-28 | 2021-09-14 | 中冶华天工程技术有限公司 | Blast furnace gas dust interception, dry dechlorination and hydrolysis conversion integrated tower |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN113388423A (en) | Blast furnace gas dust interception, dry dechlorination and hydrolysis conversion integrated tower | |
CN215250664U (en) | Multifunctional integrated tower for blast furnace gas | |
CN107739771A (en) | Coal gas of converter heat energy full-dry method purifying recovery method and its device | |
CN111992006A (en) | Blast furnace gas dust interception and dry dechlorination device | |
CN204543929U (en) | Smoke eliminator | |
CN107998817B (en) | Single tower type fume purifier flue gas purification method | |
CN105004189A (en) | Flue gas collecting and purifying device of mobile tunnel kiln | |
CN203144120U (en) | Continuous sealing slagging device for boiling chlorination furnace | |
CN104031688B (en) | The continuous pressure release Slagoff method of slag tap pressurized-gasification furnace and system thereof | |
CN207169659U (en) | A kind of Novel SCR Benitration reactor | |
CN2376992Y (en) | Turbulent flue gas purifying tower | |
CN212236678U (en) | Blast furnace gas dust interception and dry dechlorination device | |
CN202380017U (en) | Secondary dust removal system for converters | |
CN202465751U (en) | Dry dust-removing and dechlorinating composite device for blast furnace coal gas | |
CN105154142A (en) | Fluidized bed gasification device and fluidized bed gasification system | |
CN102218248B (en) | Coal gas dust collector | |
CN107335389A (en) | A kind of Novel SCR Benitration reactor | |
CN203598554U (en) | Tilted-plate-type slag-water separation device | |
CN106964213A (en) | A kind of modular radial dedusting Benitration reactor | |
CN104511192A (en) | Inclined plate type slag water separation device | |
CN206600831U (en) | Desulfurizing tower and chimney combined into one apparatus | |
CN111944564A (en) | Blast furnace gas dust removal and hydrolysis integrated desulfurization system | |
CN208620340U (en) | A kind of fluidized-bed combustion boiler gas conveying desulfurizer | |
CN109135841B (en) | Spray alkali washing tower | |
CN206553569U (en) | Ou Ye stove stock gas dust arresters |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |