CN105417174A - Novel tower-type fluidization tray - Google Patents
Novel tower-type fluidization tray Download PDFInfo
- Publication number
- CN105417174A CN105417174A CN201510981944.6A CN201510981944A CN105417174A CN 105417174 A CN105417174 A CN 105417174A CN 201510981944 A CN201510981944 A CN 201510981944A CN 105417174 A CN105417174 A CN 105417174A
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- CN
- China
- Prior art keywords
- type
- tower
- ring
- inlet pipe
- baffle plate
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- 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.)
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
The invention relates to a novel tower-type fluidization tray which comprises an elliptical head, an air inlet pipe, a baffle and a tower-type fluidization device, wherein the elliptical head is a semi-closed cavity; the air inlet pipe penetrates the sealed end of the elliptical head and extends into the elliptical head; the baffle is mounted in the elliptical head and located over an air outlet of the air inlet pipe; and the tower-type fluidization device is mounted at the open end of the elliptical head. According to the design, compressed air is conveyed into the elliptical head, passes through the center holes of fluidization plates of the tower-type fluidization device and finally flows out from a gap (fluidization surface) between the two layers of fluidization plates to play a fluidization role.
Description
Technical field
The present invention relates to a kind of fluidizer, particularly a kind of novel tower-type fluidized disk.
Background technology
Tower fluidized disk is a kind of Novel fluidization device, and it is the loose unpacked material pressurization fluidisation conveying such as aim at top-guiding type storehouse pumping system, agstone first-level transport system, bed material add sand system and designs; The fluidised form device of old-fashioned fluidized disk is canvas, feed back according to many field engineerings, employing canvas designs, often there is the phenomenons such as canvas space blocks, easy to wear, fluidisation is insufficient, often cause solid accumulation in transmitting apparatus, system cannot be run, and brings immense pressure to whole project unit operation; So design a kind of novel tower-type fluidized disk just seem particularly important to solve above-mentioned technical matters.
Summary of the invention
To the defect that above-mentioned background technology exists, the problem to be solved in the present invention be by compressed air delivery in ellipse head, through the fluidized plate centre hole of tower fluidised form device, finally appear, to play rheomorphism from the gap (fluidisation face) of the two-layer fluidized plate of tower fluidised form device; A kind of novel tower-type fluidized disk is provided.
For solving above-mentioned technical matters, structure of the present invention comprises
Ellipse head, described ellipse head is semienclosed cavity,
Air inlet pipe, described air inlet pipe stretches to its inside through the sealed end of ellipse head,
Baffle plate, described baffle plate is arranged in ellipse head, and described baffle plate is positioned at directly over air inlet pipe air outlet,
Tower fluidised form device, described tower fluidised form device is arranged on the open end of ellipse head, described tower fluidised form device is connected to form successively from top to bottom by the ring-type gasification board of four pieces of different sizes, in described adjacent two pieces of ring-type gasification boards, the outside dimension of upper strata ring-type gasification board is greater than the internal diameter size of lower floor's ring-type gasification board, also be provided with packing ring between described adjacent two pieces of ring-type gasification boards, described packing ring makes there is gap between two pieces of adjacent ring-type gasification boards.
Further: described baffle plate is in being " U " type, and the baffle plate of described " U " type is connected on ellipse head by the side plate of both sides, and the air outlet of described air inlet pipe is just to the base plate of " U " type baffle plate.
Further again: the area of the base plate of described " U " type baffle plate is greater than the area of air inlet pipe air outlet.
Further again: described undermost ring-type gasification board passes through the open end of Flange joint at ellipse head of both sides.
Further again: the gap between described adjacent two pieces of ring-type gasification boards is 1 to 4mm.
Adopt after said structure, the present invention by compressed air delivery in ellipse head, through the fluidized plate centre hole of tower fluidised form device, finally appear, to play rheomorphism from the gap (fluidisation face) of the two-layer fluidized plate of tower fluidised form device; And the tower fluidised form device in the present invention is provided with three fluidisation faces, and three fluidisation faces evenly superpose, each fluidisation surface currentization is even, and the overall fluidisation of fluidized disk is abundant, serve not easily block, fluid effect is good and carry and act on smoothly.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the present invention is further detailed explanation.
Fig. 1 is structural representation of the present invention.
Fig. 2 is the enlarged drawing of A in Fig. 1.
Detailed description of the invention
A kind of novel tower-type fluidized disk as shown in Figure 1, comprise ellipse head 1, air inlet pipe 5, baffle plate 6 and tower fluidised form device 3, described ellipse head 1 is semienclosed cavity, described air inlet pipe 5 stretches to its inside through the sealed end of ellipse head 1, described baffle plate 6 is arranged in ellipse head 1, described baffle plate 6 is positioned at directly over air inlet pipe 5 air outlet, described tower fluidised form device 3 is arranged on the open end of ellipse head 1, described baffle plate 6 is in being " U " type, the baffle plate 6 of described " U " type is connected on ellipse head 1 by the side plate of both sides, the air outlet of described air inlet pipe 5 is just to the base plate of " U " type baffle plate 6, the area of the base plate of described " U " type baffle plate 6 is greater than the area of air inlet pipe 5 air outlet, the area of the base plate of described " U " type baffle plate 6 is greater than the area of air inlet pipe 5 air outlet.The design is transported to pressurized air in ellipse head 1 by air inlet pipe 5, through the fluidized plate centre hole of tower fluidised form device 3, finally appears from the gap (fluidisation face) of the two-layer fluidized plate of tower fluidised form device 3, to play rheomorphism.
Tower fluidised form device 3 is as depicted in figs. 1 and 2 connected to form successively from top to bottom by the ring-type gasification board of four pieces of different sizes, in described adjacent two pieces of ring-type gasification boards, the outside dimension of upper strata ring-type gasification board is greater than the internal diameter size of lower floor's ring-type gasification board, also be provided with packing ring 4 between described adjacent two pieces of ring-type gasification boards, described packing ring 4 makes there is gap between two pieces of adjacent ring-type gasification boards.Tower fluidised form device in the present invention is provided with three fluidisation faces, and three fluidisation faces evenly superpose, and each fluidisation surface currentization is even, and the overall fluidisation of fluidized disk is abundant, serve not easily block, fluid effect is good and carry and act on smoothly.
Gap between adjacent two pieces of ring-type gasification boards is as shown in Figure 11 to 4mm, and fluidisation face of the present invention gap length design according to the physical property of different material, play not easily block, fluid effect is good and carry and act on smoothly.And fluidised form device integral structure is steel structure, not easy to wear, long service life.
Claims (5)
1. a novel tower-type fluidized disk, is characterized in that: comprise
Ellipse head (1), described ellipse head (1) is semienclosed cavity,
Air inlet pipe (5), described air inlet pipe (5) stretches to its inside through the sealed end of ellipse head 1,
Baffle plate (6), described baffle plate (6) is arranged in ellipse head (1), and described baffle plate (6) is positioned at directly over air inlet pipe (5) air outlet,
Tower fluidised form device (3), described tower fluidised form device (3) is arranged on the open end of ellipse head (1), described tower fluidised form device (3) is connected to form successively from top to bottom by the ring-type gasification board of four pieces of different sizes, in described adjacent two pieces of ring-type gasification boards, the outside dimension of upper strata ring-type gasification board is greater than the internal diameter size of lower floor's ring-type gasification board, also be provided with packing ring (4) between described adjacent two pieces of ring-type gasification boards, described packing ring (4) makes there is gap between two pieces of adjacent ring-type gasification boards.
2. a kind of novel tower-type fluidized disk according to claim 1, it is characterized in that: described baffle plate (6) is in being " U " type, the baffle plate (6) of described " U " type is connected on ellipse head (1) by the side plate of both sides, and the air outlet of described air inlet pipe (5) is just to the base plate of " U " type baffle plate (6).
3. a kind of novel tower-type fluidized disk according to claim 2, is characterized in that: the area of the base plate of described " U " type baffle plate (6) is greater than the area of air inlet pipe (5) air outlet.
4. a kind of novel tower-type fluidized disk according to claim 1, is characterized in that: described undermost ring-type gasification board is connected to the open end of ellipse head (1) by the flange (2) of both sides.
5. a kind of novel tower-type fluidized disk according to claim 1, is characterized in that: the gap between described adjacent two pieces of ring-type gasification boards is 1 to 4mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510981944.6A CN105417174A (en) | 2015-12-22 | 2015-12-22 | Novel tower-type fluidization tray |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510981944.6A CN105417174A (en) | 2015-12-22 | 2015-12-22 | Novel tower-type fluidization tray |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105417174A true CN105417174A (en) | 2016-03-23 |
Family
ID=55495803
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510981944.6A Pending CN105417174A (en) | 2015-12-22 | 2015-12-22 | Novel tower-type fluidization tray |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105417174A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1257816A (en) * | 1967-12-29 | 1971-12-22 | ||
| CN2729012Y (en) * | 2004-09-20 | 2005-09-28 | 岳波 | Device for conveying granular material |
| CN204453828U (en) * | 2015-01-23 | 2015-07-08 | 上海隆麦机械设备工程有限公司 | The adjustable fluidization transmitter of pneumatic material conveying system |
| CN205367133U (en) * | 2015-12-22 | 2016-07-06 | 江苏久晟环保设备有限公司 | Novel tower fluidization dish |
-
2015
- 2015-12-22 CN CN201510981944.6A patent/CN105417174A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1257816A (en) * | 1967-12-29 | 1971-12-22 | ||
| CN2729012Y (en) * | 2004-09-20 | 2005-09-28 | 岳波 | Device for conveying granular material |
| CN204453828U (en) * | 2015-01-23 | 2015-07-08 | 上海隆麦机械设备工程有限公司 | The adjustable fluidization transmitter of pneumatic material conveying system |
| CN205367133U (en) * | 2015-12-22 | 2016-07-06 | 江苏久晟环保设备有限公司 | Novel tower fluidization dish |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160323 |