CN209740208U - Ash mixer for internal bypass turbulent flow dense-phase pneumatic conveying system - Google Patents
Ash mixer for internal bypass turbulent flow dense-phase pneumatic conveying system Download PDFInfo
- Publication number
- CN209740208U CN209740208U CN201821999406.5U CN201821999406U CN209740208U CN 209740208 U CN209740208 U CN 209740208U CN 201821999406 U CN201821999406 U CN 201821999406U CN 209740208 U CN209740208 U CN 209740208U
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- grey
- pipe
- ash
- defeated
- ware body
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Abstract
The utility model relates to a mix grey ware, especially relate to an interior bypass turbulent flow dense phase pneumatic conveying system is with mixing grey ware, including mixing grey ware body, mix the inside defeated ash pipe that is equipped with of grey ware body, mix grey ware body one end and pass through defeated grey female pipe of defeated ash union coupling, mix the grey ware body other end and connect and defeated grey union coupling through a shrinkage, it has a plurality of slant water conservancy diversion strips to weld with the round steel on the defeated grey pipe, be connected with the intake pipe on mixing grey ware body lateral wall, mix grey ware body, defeated grey pipe and shrinkage and connect between forming gaseous cavity. The utility model discloses an intake pipe lets in the air and increases the defeated air output, makes the ash intensive mixing that air and defeated ash pipe carried, adjusts grey gas to appropriate concentration ratio, improves conveying capacity, eliminates "stifled pipe" and sprouts the state for carry smoothly, not stifled pipe.
Description
Technical Field
The utility model relates to an ash mixer especially relates to an interior bypass turbulent flow dense phase pneumatic conveying system is with mixing ash ware.
Background
China introduces and develops a pneumatic ash removal system from the middle of seventies and is widely applied to a power system, but a plurality of problems are exposed in the actual engineering operation: the ash-gas conveying ratio is low. The pipe is easy to block. The medium flow velocity in the pipeline is high, the pipeline and the valve are seriously abraded, and the operation and maintenance cost is high. The system has small output and poorer economy when the system is transported for a long distance. The pipeline is many, takes up an area of more, arranges the difficulty, and the system reliability is relatively poor.
An internal bypass (double-sleeve) pneumatic conveying system is an advanced pneumatic conveying technology developed abroad in the 80 th century. The developed internal bypass turbulent dense-phase pneumatic conveying system changes the working conditions of low concentration, high flow speed, high abrasion, easy pipe blockage and high energy consumption in conventional positive-pressure conveying, finds an ideal alternative scheme for solving the problems of high output and dense-phase conveying of high-abrasion materials, and completely realizes the localization. The inner bypass ash conveying pipeline and various valves and pipeline accessories arranged on the pipeline jointly form a set of complete inner bypass turbulent flow dense-phase pneumatic conveying system. The ash mixer is a key pipeline accessory.
SUMMERY OF THE UTILITY MODEL
The utility model discloses a solve the defect that exists among the above-mentioned prior art and be not enough, provide one kind and adopt the intake pipe to let in the air and increase the defeated air output, make the grey intensive mixing that air and defeated ash pipe carried, adjust grey gas to appropriate concentration ratio, improve conveying capacity, eliminate "stifled pipe" and be in the bud state for carry smoothly, the interior bypass turbulent flow dense phase pneumatic conveying system who does not stifled pipe is with mixing grey ware.
The technical scheme of the utility model: the utility model provides an interior bypass turbulent flow dense phase pneumatic conveyor system is with mixing grey ware, is including mixing grey ware body, mix the inside defeated ash pipe that is equipped with of grey ware body, mix grey ware body one end and pass through defeated grey female pipe of defeated union coupling, mix the grey ware body other end and connect and defeated grey union coupling through a shrinkage, the last circular steel welding that has a plurality of slant water conservancy diversion strips that has of defeated grey pipe, be connected with the intake pipe on mixing grey ware body lateral wall, mix grey ware body, defeated grey pipe and shrinkage and connect between formation gas cavity.
Preferably, the ash mixer body is a horizontally arranged seamless pipe, the air inlet pipe is vertically connected to the ash mixer body, and the contraction joint is welded on the ash mixer body.
Preferably, the top of the air inlet pipe is provided with an air inlet pipe connecting flange, and two ends of the ash conveying pipe are provided with ash conveying pipe connecting flanges.
Preferably, one end of the ash mixer body is connected with the ash conveying pipe through a connecting ring.
Preferably, the length of the oblique flow guide strip is matched with the length of the gas chamber.
The utility model discloses well intake pipe passes through intake pipe flange and air supply pipe connection, and defeated ash pipe passes through defeated ash union coupling flange and defeated grey female union coupling. The pipeline flanges are connected by flanges, so that the installation and the maintenance are convenient. The temperature difference of the main ash conveying pipeline is basically stable, the thermal expansion and the cold shrinkage are reduced, the flange connection is leak-free, and the safety and the reliability are realized.
The utility model provides an ash conveying pipe is actually for mixing the ash inlet of ash ware, and the ash in the ash conveying main pipe is sent into through ash conveying pipe and is mixed the ash ware. The ash conveying pipe is welded with a guide strip with a certain inclination by round steel. The gas entering the ash mixer from the gas inlet pipe flows to the outlet of the ash mixer along the diversion strips, and is mixed (contracted and connected) with the fly ash sent by the ash conveying pipe at the outlet of the ash mixer. The guide strips arranged on the ash conveying pipe enable compressed air entering the ash mixer to flow to the outlet of the ash mixer along a certain inclination angle on one hand, and increase the disturbance of air flow on the other hand, so that the compressed air and fly ash are in a flowing state after being mixed.
The contraction joint increases the air flow speed of the obtained air chamber, forms certain impact and fluidization effect on fly ash, pushes the air-ash mixture to flow forward, and prevents pipe blockage.
The utility model discloses an intake pipe lets in the air and increases the defeated air output, makes the ash intensive mixing that air and defeated ash pipe carried, adjusts grey gas to appropriate concentration ratio, improves conveying capacity, eliminates "stifled pipe" and sprouts the state for carry smoothly, not stifled pipe.
Drawings
Fig. 1 is a schematic structural view of the present invention;
In the figure, 1, an air inlet pipe connecting flange, 2, an air inlet pipe, 3, an ash conveying pipe connecting flange, 4, an ash conveying pipe, 5, an inclined flow guide strip, 6, a gas chamber, 7, a contraction joint, 8, an ash mixer body and 9, a connecting ring are arranged.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings, but the present invention is not limited thereto.
As shown in figure 1, an interior bypass turbulent flow dense phase pneumatic conveying system is with mixing grey ware, including mixing grey ware body 8, mix grey ware body 8 inside and be equipped with defeated ash pipe 4, mix grey ware body 8 one end and pass through defeated grey female pipe of defeated ash pipe 4 connection, mix grey ware body 8 other end and connect 7 and defeated grey pipe 4 through a shrinkage, have a plurality of slant water conservancy diversion strips 5 with round steel welding on the defeated ash pipe 4, be connected with intake pipe 2 on mixing grey ware body 8 lateral wall, mix grey ware body 8, defeated grey pipe 4 and the shrinkage and connect and form gas cavity 6 between 7. Mix grey ware body 8 and be the seamless pipe of a level setting, intake pipe 2 is vertical to be connected on mixing grey ware body 8, and the welding of contraction joint 7 is on mixing grey ware body 8. The top of the air inlet pipe 2 is provided with an air inlet pipe connecting flange 1, and two ends of the ash conveying pipe 4 are provided with ash conveying pipe connecting flanges 3. One end of the ash mixer body 8 is connected with the ash conveying pipe 4 through a connecting ring 9. The length of the oblique flow guide strip 5 is matched with that of the gas chamber 6.
Mix grey ware body both ends and pass through defeated grey pipe and defeated grey union coupling flange and defeated grey female pipe both ends flange joint, intake pipe and for the transport trachea pass through intake pipe flange joint, and the intake pipe orientation is installed during the installation in the intake pipe, reduces gas ash mixture commodity circulation and goes into trachea shutoff valve and pipeline annex.
The ash mixing device, the air valve group for mixing ash and the instrument electric control equipment form a complete ash mixing system to meet the regulation of the ash-air ratio of the ash conveying pipeline and prevent the ash conveying main pipe from blocking the pipe. The main valve and the auxiliary valve of the air valve group control the two groups of air pipelines for mixing ash. The pressure transmitter is arranged on the ash conveying main pipe behind the ash mixer and the air valve group air pipe for mixing ash, when ash is normally conveyed, the air valve for the main ash mixer is opened to meet the conveying requirement, when the abnormal ash conveying concentration of the system is too high, the conveying pressure is increased to a designed preset value, the air valve for the auxiliary ash mixer is automatically opened by the ash mixing system, the conveying air quantity is increased, the ash gas is adjusted to a proper concentration ratio, the conveying capacity is improved, the 'blocked pipe' is eliminated in a bud state, and the on-site occurrence of the blocked pipe is prevented.
Claims (5)
1. The utility model provides an interior bypass turbulent dense phase air conveying system is with mixing grey ware, includes the ash mixer body, its characterized in that: mix grey ware body inside and be equipped with defeated ash pipe, mix grey ware body one end and pass through defeated grey female pipe of defeated grey union coupling, mix grey ware body other end and connect and defeated grey union coupling through a shrinkage, it has a plurality of slant water conservancy diversion strips to weld with the round steel on the defeated grey pipe, be connected with the intake pipe on mixing grey ware body lateral wall, mix grey ware body, defeated grey pipe and shrinkage and connect and form gaseous cavity between.
2. The ash mixer for the internal bypass turbulent dense-phase pneumatic conveying system according to claim 1, wherein: mix grey ware body and be the seamless pipe of a level setting, the vertical connection of intake pipe is on mixing grey ware body, the welding of shrinkage joint is on mixing grey ware body.
3. The ash mixer for the internal bypass turbulent dense-phase pneumatic conveying system according to claim 1, wherein: the top of the air inlet pipe is provided with an air inlet pipe connecting flange, and two ends of the ash conveying pipe are provided with ash conveying pipe connecting flanges.
4. the ash mixer for the internal bypass turbulent dense-phase pneumatic conveying system according to claim 1, wherein: one end of the ash mixing device body is connected with the ash conveying pipe through a connecting ring.
5. The ash mixer for the internal bypass turbulent dense-phase pneumatic conveying system according to claim 1, wherein: the length of the oblique flow guide strip is matched with that of the gas chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821999406.5U CN209740208U (en) | 2018-11-30 | 2018-11-30 | Ash mixer for internal bypass turbulent flow dense-phase pneumatic conveying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821999406.5U CN209740208U (en) | 2018-11-30 | 2018-11-30 | Ash mixer for internal bypass turbulent flow dense-phase pneumatic conveying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209740208U true CN209740208U (en) | 2019-12-06 |
Family
ID=68700250
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821999406.5U Expired - Fee Related CN209740208U (en) | 2018-11-30 | 2018-11-30 | Ash mixer for internal bypass turbulent flow dense-phase pneumatic conveying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209740208U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116767820A (en) * | 2023-08-22 | 2023-09-19 | 山西冠力法兰股份有限公司 | Ejection conveying device |
-
2018
- 2018-11-30 CN CN201821999406.5U patent/CN209740208U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116767820A (en) * | 2023-08-22 | 2023-09-19 | 山西冠力法兰股份有限公司 | Ejection conveying device |
| CN116767820B (en) * | 2023-08-22 | 2023-11-24 | 山西冠力法兰股份有限公司 | Ejection conveying device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20191206 Termination date: 20211130 |