CN211635996U - Inlet blowing-assisting system of semi-dry desulfurization tower - Google Patents
Inlet blowing-assisting system of semi-dry desulfurization tower Download PDFInfo
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- CN211635996U CN211635996U CN201922214797.6U CN201922214797U CN211635996U CN 211635996 U CN211635996 U CN 211635996U CN 201922214797 U CN201922214797 U CN 201922214797U CN 211635996 U CN211635996 U CN 211635996U
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Abstract
The utility model discloses a semidry process desulfurizing tower entry helps blows system, including the desulfurizing tower main part with vertically help the blowing pipeline, the interior wallboard is installed to the below of desulfurizing tower main part, and the below of interior wallboard installs and transversely helps the blowing pipeline, vertically help the middle part that the blowing pipeline is located horizontal help the blowing pipeline rear end. This semi-dry process desulfurizing tower entry helps blows system sets up behind the blowing aid device, blow in the absorption tower with the dust in the absorption tower entry flue department flue gas, reduce entry flue dust gathering, flue blockage has been avoided, the draught fan jump stops, the emergence of the condition such as boiler flame-out, thereby effectively avoid the formation to the deposition, and help and blow the device and adopt the carbon steel, the low price, practice thrift the cost than the extension flue, save space, more safe and reliable, if there is the deposition gathering, through helping the blowing, blow in the absorption tower with this part deposition, join flue gas system again, can not influence the stability and the normal operating of system.
Description
Technical Field
The utility model relates to a desulfurizing tower technical field specifically is semi-dry desulfurization tower entry helps blows system.
Background
In the semi-dry desulfurization tower without the blowing-assisting system, because the resistance of a concave part at the inlet of the absorption tower is larger, part of dust in the flue gas from the boiler can be accumulated when the flue gas passes through the concave part, if the ash can not be removed in time, more and more dust is accumulated to block the flue at the inlet of the absorption tower, and in case of serious conditions, the induced draft fan is stopped, and the boiler is flamed out. In order to compensate the defects, resistance is reduced by means of lengthening the length of a flue at the entrance of the concave part and the like, so that material loss is high, and the occupied area is increased.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a semidry process desulfurizing tower entry helps blows system to propose the flue for the spill in solving above-mentioned background art, the flue gas resistance is great, the problem of the ash that easily falls.
In order to achieve the above object, the utility model provides a following technical scheme: the inlet blowing-assisting system for the semi-dry desulfurization tower comprises a desulfurization tower main body and a longitudinal blowing-assisting pipeline, wherein an inner wall plate is arranged below the desulfurization tower main body, a transverse blowing-assisting pipeline is arranged below the inner wall plate, and the longitudinal blowing-assisting pipeline is positioned in the middle of the rear end of the transverse blowing-assisting pipeline.
Preferably, the transverse blowing-assisting pipelines are uniformly distributed along the central axis direction of the longitudinal blowing-assisting pipeline, the distance between the transverse blowing-assisting pipelines is 350mm, and three groups of three transverse blowing-assisting pipelines are arranged.
Preferably, the outer part of the transverse blowing-assisting pipeline is of an n-shaped structure, and the depth of the transverse blowing-assisting pipeline penetrating through the desulfurizing tower main body is 30 mm.
Preferably, the transverse blowing-assisted pipeline and the longitudinal blowing-assisted pipeline are both made of carbon steel, the diameter of the inner wall of the transverse blowing-assisted pipeline is 10mm, and the width diameter of the inner wall of the longitudinal blowing-assisted pipeline is 20 mm.
Preferably, the longitudinal blowing-assisting pipelines are uniformly distributed along the bottom surface wall of the inner wall plate, the distance between every two adjacent longitudinal blowing-assisting pipelines is 600mm, the number of the longitudinal blowing-assisting pipelines is four, and the longitudinal blowing-assisting pipelines are parallel to each other.
Compared with the prior art, the beneficial effects of the utility model are as follows: blowing dust in flue gas at an inlet flue of the absorption tower into the absorption tower; reducing the dust accumulation of the inlet flue; the invention avoids the occurrence of the conditions of flue blockage, the jump stop of an induced draft fan, the flameout of a boiler and the like, and can mainly blow the dust in the flue gas at the inlet of the absorption tower into the absorption tower so as to reduce the dust accumulation of the inlet flue;
1. after the auxiliary blowing system is added, the utility model is equivalent to strengthening the air flow, so that the deposited dust falling at the inlet is added into the flue gas system again and enters the absorption tower, thereby effectively avoiding the dust falling at the inlet of the absorption tower, enabling the system to run more stably and avoiding worrying about the blockage of the inlet flue;
2. the utility model discloses after the setting helped the blowing device, can effectively avoid the formation to the deposition. The blowing assisting device is made of carbon steel, is low in price, saves cost compared with a lengthened flue, saves space, is safe and reliable, blows the accumulated dust into the absorption tower through blowing assisting if the accumulated dust is accumulated, and does not influence the stability and normal operation of the system by adding the smoke system again.
Drawings
FIG. 1 is a schematic view of the structure of the present invention;
FIG. 2 is a schematic view of the connection structure between the transverse blowing-assisted pipeline and the longitudinal blowing-assisted pipeline of the present invention;
fig. 3 is a schematic view of the connection structure between the inner wall plate and the horizontal blowing-assisting pipeline of the present invention.
In the figure: 1. a main body of the desulfurizing tower; 2. an inner wall panel; 3. a transverse blowing-assisting pipeline; 4. and (4) longitudinally blowing-assisted pipelines.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-3, the present invention provides a technical solution: the inlet blowing-assisted system for the semi-dry desulfurization tower comprises a desulfurization tower main body 1 and a longitudinal blowing-assisted pipeline 4, wherein an inner wall plate 2 is arranged below the desulfurization tower main body 1, a transverse blowing-assisted pipeline 3 is arranged below the inner wall plate 2, the outer part of the transverse blowing-assisted pipeline 3 is of an n-shaped structure, and the depth of the transverse blowing-assisted pipeline 3 penetrating through the desulfurization tower main body 1 is 30 mm;
the longitudinal blowing-assisting pipelines 4 are located in the middle of the rear end of the transverse blowing-assisting pipeline 3, the transverse blowing-assisting pipeline 3 is uniformly distributed along the axis direction of the longitudinal blowing-assisting pipeline 4, the distance between the transverse blowing-assisting pipelines 3 is 350mm, three groups of transverse blowing-assisting pipelines 3 are arranged, each group is three, the transverse blowing-assisting pipeline 3 and the longitudinal blowing-assisting pipeline 4 are both made of carbon steel, the diameter of the inner wall of the transverse blowing-assisting pipeline 3 is 10mm, the width diameter of the inner wall of the longitudinal blowing-assisting pipeline 4 is 20mm, the longitudinal blowing-assisting pipeline 4 is uniformly distributed along the bottom surface wall of the inner wall plate 2, the distance between the longitudinal blowing-assisting pipelines 4 is 600mm, four longitudinal blowing-assisting pipelines 4 are arranged, and the longitudinal blowing-assisting pipelines 4 are parallel to each other.
The working principle is as follows: when the inlet blowing-assisting system for the semi-dry desulfurization tower is used, firstly, the flue gas generated inside the desulfurization tower main body 1 can flow into the transverse blowing-assisting pipeline 3 in sequence, the transverse blowing-assisting pipeline 3 is connected with the longitudinal blowing-assisting pipeline 4, so that the flue gas can be guided into the longitudinal blowing-assisting pipeline 4, at the moment, the flue gas can flow along the inside of the longitudinal blowing-assisting pipeline 4, the flue gas can be discharged, and the blanking speed of the desulfurization tower main body 1 can be effectively improved.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (5)
1. Semi-dry desulfurization tower entry blowing-assisted system, including desulfurizing tower main part (1) and vertical blowing-assisted pipeline (4), its characterized in that: inner wall plates (2) are installed below the desulfurizing tower main body (1), transverse blow-assisting pipelines (3) are installed below the inner wall plates (2), and the longitudinal blow-assisting pipelines (4) are located in the middle of the rear ends of the transverse blow-assisting pipelines (3).
2. The semi-dry desulfurization tower inlet blowing-assisted system according to claim 1, characterized in that: the transverse blowing-assisting pipelines (3) are uniformly distributed along the central axis direction of the longitudinal blowing-assisting pipeline (4), the distance between the transverse blowing-assisting pipelines (3) is 350mm, and three groups of three transverse blowing-assisting pipelines (3) are arranged.
3. The semi-dry desulfurization tower inlet blowing-assisted system according to claim 1, characterized in that: the outer part of the transverse blowing-assisting pipeline (3) is of an n-shaped structure, and the depth of the transverse blowing-assisting pipeline (3) penetrating through the desulfurizing tower main body (1) is 30 mm.
4. The semi-dry desulfurization tower inlet blowing-assisted system according to claim 1, characterized in that: the transverse blowing-assisting pipeline (3) and the longitudinal blowing-assisting pipeline (4) are made of carbon steel, the diameter of the inner wall of the transverse blowing-assisting pipeline (3) is 10mm, and the width diameter of the inner wall of the longitudinal blowing-assisting pipeline (4) is 20 mm.
5. The semi-dry desulfurization tower inlet blowing-assisted system according to claim 1, characterized in that: the longitudinal blowing-assisting pipelines (4) are uniformly distributed along the bottom surface wall of the inner wallboard (2), the distance between the longitudinal blowing-assisting pipelines (4) is 600mm, four longitudinal blowing-assisting pipelines (4) are arranged, and the longitudinal blowing-assisting pipelines (4) are parallel to each other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922214797.6U CN211635996U (en) | 2019-12-11 | 2019-12-11 | Inlet blowing-assisting system of semi-dry desulfurization tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922214797.6U CN211635996U (en) | 2019-12-11 | 2019-12-11 | Inlet blowing-assisting system of semi-dry desulfurization tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211635996U true CN211635996U (en) | 2020-10-09 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922214797.6U Active CN211635996U (en) | 2019-12-11 | 2019-12-11 | Inlet blowing-assisting system of semi-dry desulfurization tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211635996U (en) |
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2019
- 2019-12-11 CN CN201922214797.6U patent/CN211635996U/en active Active
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Blowing aid system at the inlet of semi dry desulfurization tower Effective date of registration: 20210719 Granted publication date: 20201009 Pledgee: China Construction Bank Corporation Nanjing Jianye sub branch Pledgor: NANJING DINGHUAN NEW ENERGY SCIENCE AND TECHNOLOGY Co.,Ltd. Registration number: Y2021980006342 |