CN105966921A - Material issuing device for powdered solid and gas conveying - Google Patents
Material issuing device for powdered solid and gas conveying Download PDFInfo
- Publication number
- CN105966921A CN105966921A CN201610573381.1A CN201610573381A CN105966921A CN 105966921 A CN105966921 A CN 105966921A CN 201610573381 A CN201610573381 A CN 201610573381A CN 105966921 A CN105966921 A CN 105966921A
- Authority
- CN
- China
- Prior art keywords
- solid
- gas
- pipe
- feed opening
- high pressure
- 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.)
- Pending
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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
- B65G53/40—Feeding or discharging devices
- B65G53/50—Pneumatic devices
-
- 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
- B65G53/52—Adaptations of pipes or tubes
- B65G53/526—Adaptations of pipes or tubes with means for special treatment to facilitate transport
-
- 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
- B65G2201/00—Indexing codes relating to handling devices, e.g. conveyors, characterised by the type of product or load being conveyed or handled
- B65G2201/04—Bulk
- B65G2201/042—Granular material
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Air Transport Of Granular Materials (AREA)
Abstract
A material issuing device for powdered solid and gas conveying comprises a high pressure gas injection pipe, a solid feed opening, a gas-solid mixing chamber and a gas-solid two-phase mixing jetting pipe which are connected into a whole. The high pressure gas injection pipe, the gas-solid mixing chamber and the gas-solid two-phase mixing jetting pipe are located on a same central axis, the gas-solid mixing chamber is formed between the high pressure gas injection pipe and the gas-solid two-phase mixing jetting pipe, the solid feed opening is located above the gas-solid mixing chamber, and the gas-solid mixing chamber is communicated with the high pressure gas injection pipe, the solid feed opening and the gas-solid two-phase mixing jetting pipe. The high pressure gas injection pipe is a gradually necked type injection pipe, and the gas-solid two-phase mixing jetting pipe is a gradually expanding type jetting pipe. The material issuing device for powdered solid and gas conveying effectively improves the conveying capacity.
Description
Technical field
The present invention relates to a kind of issuance of materials device, especially a kind of for granular solid strength
The issuance of materials device of conveying.
Background technology
Issuance of materials device is the key equipment that in air-transport system, feed uses, owing to it has
Advantage is widely used to have structure relatively easy, easy to maintenance etc..Air conveying transmitter
It it is the key utilizing compressed gas as transferring working medium to carry granular solid particle
Equipment.It is to utilize compressed-air actuated static energy, by having a special construction
Tract, static energy is changed into dynamic pressure energy, the gas dynamic pressure energy that will convert in issuance of materials device
Pass to solid particle, make solid particle suspend, accelerate, be brought into conveying mother simultaneously
Pipe.Conventional issuance of materials device be all by solid material feeding mouth, gas nozzle, receiving chamber,
Mixing tube and anemostat (also can be without) composition.When the higher gas of static pressure is by spraying
Mouth sprays through narrow and small tract, and gas flow rate is very big, and (Mach number is left up to 0.5
Right), after then gas enters the tract of less expansion angle, gas turbulence effect is high
Degree development, produces negative pressure in pipeline throat.Solid particle is sucked under suction function
Enter blanking chamber, and then realize gas-particle two-phase mixing, energy exchange occurs therebetween,
Solid is accelerated, and gas is decelerated, and the two sliding velocity is greatly reduced, but can simultaneously
Cause a large amount of energy loss.Owing to conventional blanking device exists the defect of design aspect, make
Become gas-particle two-phase mixing uneven, greatly reduce the transmitting capacity of issuance of materials device.Simultaneously
Owing to mixing chamber design exists drawback, there is a large amount of flow dead in often making it, make
Becoming solid material prolonged stay, the solid stronger for water absorption easily lumps, and causes
The internal blocking of issuance of materials device.Some issuance of materials device can make flowing not due to design unreasonable structure
Uniformly, the phenomenons such as some regional area abrasion increase are caused.
Summary of the invention
In order to overcome drawbacks described above, the present invention provides a kind of for granular solid strength
The issuance of materials device of conveying, the described issuance of materials device air conveying for granular solid promotes to be sent out
Send ability, stable, energy consumption is relatively low.
The present invention is to solve that its technical problem be the technical scheme is that a kind of use
In the issuance of materials device that granular solid is air conveying, including the gases at high pressure connected as one
Spray into pipe, solid feed opening, gas-solid mixing room and gas-particle two-phase mixing bleed pipe, institute
State gases at high pressure spray into pipe, gas-solid mixing room and gas-particle two-phase bleed pipe be in same in
On mandrel line, gas-solid mixing room is formed at gases at high pressure and sprays into pipe and gas-particle two-phase ejection
Between pipe, solid feed opening is positioned at the top of gas-solid mixing room, and gas-solid mixing room is respectively
Spray into pipe, solid feed opening and gas-particle two-phase bleed pipe to communicate with gases at high pressure, described
It is tapering type that gases at high pressure spray into pipe, and described gas-particle two-phase mixing bleed pipe is flaring
Formula.
As a further improvement on the present invention, the central axis of described solid feed opening with
Gases at high pressure spray into the central shaft residing for pipe, gas-solid mixing room, gas-particle two-phase bleed pipe
Line is in a certain angle, and this angle is more than the internal friction angle of solid powder.
As a further improvement on the present invention, described gases at high pressure spray into pipe include conveying
Trachea connects pipeline, Flange joint dish and traction therapy that reducing pipe, described conveying trachea
Connecting pipeline to weld between Flange joint dish, described conveying trachea connects pipeline and draws
Between Fa Er reducing pipe coaxial and be threaded.
As a further improvement on the present invention, the taper angle of described traction therapy that reducing pipe is
8-15°。
As a further improvement on the present invention, the outlet of described traction therapy that reducing pipe is positioned at
The center of gas-solid mixing room.
As a further improvement on the present invention, described gas-solid mixing room and solid feed opening
Between be tangential round and smooth be connected.
As a further improvement on the present invention, described solid feed opening includes being connected as one
The feed opening flange of body and feed opening inwall, described feed opening Flange joint is in blanking bin
With between feed opening inwall, described feed opening inwall is tangentially connected with gas-solid mixing room.
As a further improvement on the present invention, described gas-solid mixing room is sprayed with gas-particle two-phase
Go out between pipe for tangential round and smooth connected.
As a further improvement on the present invention, described gas-particle two-phase bleed pipe includes connecting
Straight portion, flaring part and the end flange being integrated, described straight portion and gas
Gu mixing chamber is tangentially connected, described end flange pipe female with conveying is connected.
As a further improvement on the present invention, the flaring angle of described flaring part is
8-15°。
The invention has the beneficial effects as follows: the present invention is air conveying for granular solid
Issuance of materials device, inner chamber, for first to reduce rear diffused structure, effectively eliminates current existing confession
The suction of glassware is not enough, there is Dead space and the drawback in material lagging district, effectively carries
Rise conveying capacity.Meanwhile, the negative pressure that gas-solid mixing room produces due to la farr pipe is more
Easily make solid powder flow, so reduce Dual-Phrase Distribution of Gas olid mixing in mixing chamber and
The share of energy exchange.
Accompanying drawing explanation
Fig. 1 is the present invention for the combination of the air conveying issuance of materials device of granular solid
Figure.
Comparison the figures above, is supplemented as follows explanation:
1---gases at high pressure spray into pipe 2---solid feed opening
3---gas-solid mixing room 4---gas-particle two-phase mixing bleed pipe
11---conveying trachea connects pipeline 12---Flange joint dish
13---traction therapy that reducing pipe 21---feed opening flange
22---feed opening inwall 41---straight portion
42---flaring part 43---end flange
Detailed description of the invention
A kind of issuance of materials device air conveying for granular solid, including connecting as one
Gases at high pressure spray into pipe 1, solid feed opening 2, gas-solid mixing room 3 and gas-solid two
Mixing bleed pipe 4 mutually.Described gases at high pressure spray into pipe 1, gas-solid mixing room 3 and gas
Gu biphase bleed pipe 4 is on same central axis, gas-solid mixing room 3 is formed at height
Body of calming the anger sprays between pipe 1 and gas-particle two-phase bleed pipe 4, and solid feed opening 2 is positioned at
The top of gas-solid mixing room 3, gas-solid mixing room 3 spray into gases at high pressure respectively pipe 1,
Solid feed opening 2 and gas-particle two-phase bleed pipe 4 communicate.Described gases at high pressure spray into pipe
1 is tapering type, and described gas-particle two-phase mixing bleed pipe 4 is gradual-enlargement type.
Laval nozzle is to be made up of two conical pipes, before the first stage for shrink
Pipe, after second stage for expansion pipe.In the first stage, gasmovement is followed " flows
When body moves in pipe, little place, cross section flow velocity is big, and cross section general goal flow velocity is little " principle,
Therefore air-flow constantly accelerates.When arriving narrow larynx, flow velocity has been over velocity of sound.And
Transonic fluid is the most no longer followed when motion, and " greatly, cross section is big for little place, cross section flow velocity
Place's flow velocity is little " principle, but on the contrary, cross section is the biggest, flow velocity is the fastest, therefore,
In second stage, the speed of combustion gas stream is further accelerated, for 2-3 kilometer per second,
Be equivalent to 7-8 times of velocity of sound, this creates the terminal huge thrust.Laval nozzle
Actually serve the effect of " flow velocity enhancer ".
The central axis of described solid feed opening 2 and gases at high pressure spray into pipe 1, gas-solid
Central axis residing for mixing chamber 3, gas-particle two-phase bleed pipe 4 is in a certain angle, should
Angle is more than the internal friction angle of solid powder.That is, tangent binding pattern is used, can
Flow into rapidly in issuance of materials device with beneficially solid particle, transferred out rapidly simultaneously.
Avoiding problems in granule of some easy caking is present in issuance of materials device for a long time cause stifled
Plug phenomenon.
Described gases at high pressure spray into pipe 1 and include that carrying trachea connects pipeline 11, flange
Connection dish 12 and traction therapy that reducing pipe 13, described conveying trachea connects pipeline 11
Welding with between Flange joint dish 12, described conveying trachea connects pipeline 11 and traction therapy
Between your reducing pipe 13 coaxial and be threaded.Flange joint dish 12 for
High-pressure delivery gas tube (not shown) is connected.Described traction therapy that reducing pipe 13
Taper angle is 8-15 °.The outlet of described traction therapy that reducing pipe 13 is positioned at gas-solid mixing
The center of room 3.
Round and smooth it is connected for tangential between described gas-solid mixing room 3 and solid feed opening 2.
Feed opening flange 21 that described solid feed opening 2 includes connecting as one and under
Material mouth inwall 22, described feed opening flange 21 be connected to blanking bin (not shown) and
Between feed opening inwall 22, described feed opening inwall 22 is tangential with gas-solid mixing room 3
Connect.
It it is tangential round and smooth phase between described gas-solid mixing room 3 and gas-particle two-phase bleed pipe 4
Even.
Straight portion 41 that described gas-particle two-phase bleed pipe 4 includes connecting as one,
Flaring part 42 and end flange 43, described straight portion 41 and gas-solid mixing room 3
Tangentially connected, described end flange 43 is connected with conveying mother's pipe (not shown).Institute
The flaring angle stating flaring part 42 is 8-15 °.
Issuance of materials device inner chamber of the present invention is for first to reduce rear diffused structure, therefore, and the present invention
Issuance of materials device is la farr pipe formula issuance of materials device, thus effectively eliminates current existing loader
Suction not enough, there is Dead space and the drawback in material lagging district.Meanwhile, gas-solid
Mixing chamber 3 is more easy to make solid powder flow due to the negative pressure that la farr pipe produces, and then
Reduce Dual-Phrase Distribution of Gas olid mixing in mixing chamber and the share of energy exchange.The present invention
For granular solid air conveying la farr pipe formula issuance of materials device, conveying capacity has bigger
Improve, improve more than 20% than the most common injecting type blanking device conveying capacity.Whole
Issuance of materials device is easy to cast molding, and the most tapering type gases at high pressure spray into pipe 1, gas-solid mixes
Close and between room 3, solid feed opening 2, gradual-enlargement type gas-particle two-phase bleed pipe 4, use circle
Slipping over and cross connection, these slow down the solid particle violent journey of collision to this intra-zone
Degree and the degree of wear, not only save energy consumption but also improve the service life of issuance of materials device.
Claims (10)
1. for the issuance of materials device that granular solid is air conveying, including being connected as one
It is mixed that the gases at high pressure of body spray into pipe, solid feed opening, gas-solid mixing room and gas-particle two-phase
Closing bleed pipe, described gases at high pressure spray into pipe, gas-solid mixing room sprays with gas-particle two-phase
Pipe is on same central axis, gas-solid mixing room be formed at gases at high pressure spray into pipe and
Between gas-particle two-phase bleed pipe, solid feed opening is positioned at the top of gas-solid mixing room, gas
Gu mixing chamber sprays into pipe, solid feed opening and gas-particle two-phase ejection respectively with gases at high pressure
Pipe communicates, and it is characterized in that: it is tapering type that described gases at high pressure spray into pipe, described gas-solid
Two-phase mixtures bleed pipe is gradual-enlargement type.
The most according to claim 1 for air conveying the sending out of granular solid
Glassware, is characterized in that: the central axis of described solid feed opening sprays into gases at high pressure
Central axis residing for pipe, gas-solid mixing room, gas-particle two-phase bleed pipe is in a certain angle,
This angle is more than the internal friction angle of solid powder.
The most according to claim 1 for air conveying the sending out of granular solid
Glassware, is characterized in that: described gases at high pressure spray into pipe include carry trachea connect pipeline,
Flange joint dish and traction therapy that reducing pipe, described conveying trachea connects pipeline and flange
Welding between connection dish, described conveying trachea connects between pipeline and your reducing pipe of traction therapy
Coaxial and be threaded.
The most according to claim 3 for air conveying the sending out of granular solid
Glassware, is characterized in that: the taper angle of described traction therapy that reducing pipe is 8-15 °.
The most according to claim 3 for air conveying the sending out of granular solid
Glassware, is characterized in that: the outlet of described traction therapy that reducing pipe is positioned at gas-solid mixing room
Center.
The most according to claim 1 for air conveying the sending out of granular solid
Glassware, is characterized in that: for tangent circle between described gas-solid mixing room and solid feed opening
Sliding connected.
The most according to claim 6 for air conveying the sending out of granular solid
Glassware, is characterized in that: described solid feed opening includes the feed opening method connected as one
Orchid and feed opening inwall, described feed opening Flange joint is in blanking bin and feed opening inwall
Between, described feed opening inwall is tangentially connected with gas-solid mixing room.
The most according to claim 1 for air conveying the sending out of granular solid
Glassware, is characterized in that: for cutting between described gas-solid mixing room and gas-particle two-phase bleed pipe
It is connected to round and smooth.
The most according to claim 8 for air conveying the sending out of granular solid
Glassware, is characterized in that: it is straight that described gas-particle two-phase bleed pipe includes connecting as one
Partly, flaring part and end flange, described straight portion is tangential with gas-solid mixing room
Connecting, described end flange pipe female with conveying is connected.
The most according to claim 9 for air conveying the sending out of granular solid
Glassware, is characterized in that: the flaring angle of described flaring part is 8-15 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610573381.1A CN105966921A (en) | 2016-07-20 | 2016-07-20 | Material issuing device for powdered solid and gas conveying |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610573381.1A CN105966921A (en) | 2016-07-20 | 2016-07-20 | Material issuing device for powdered solid and gas conveying |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105966921A true CN105966921A (en) | 2016-09-28 |
Family
ID=56951908
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610573381.1A Pending CN105966921A (en) | 2016-07-20 | 2016-07-20 | Material issuing device for powdered solid and gas conveying |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105966921A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107352274A (en) * | 2017-08-25 | 2017-11-17 | 天津商业大学 | A kind of regulatable new induction Pneumatic conveyer of particle concentration |
| CN107416529A (en) * | 2017-09-08 | 2017-12-01 | 中国华能集团清洁能源技术研究院有限公司 | A kind of Contiuum type air conveyor |
| CN114148759A (en) * | 2021-12-30 | 2022-03-08 | 南京翔瑞智能装备技术有限公司 | Gas-powder conveying device without returning charge |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB903102A (en) * | 1959-06-23 | 1962-08-09 | Acme Ventilating Ltd | Improvements relating to pneumatic conveyors for loose materials |
| JPH08113369A (en) * | 1994-10-17 | 1996-05-07 | Shohei Senda | Granule supplying device |
| CN2353940Y (en) * | 1998-09-15 | 1999-12-15 | 郑德明 | Low-pressure pneumatic continuous delivery pump |
| CN201367259Y (en) * | 2009-02-25 | 2009-12-23 | 大连森雅能源环保设备有限公司 | Jet type material feeder, |
| CN201785043U (en) * | 2010-06-11 | 2011-04-06 | 西安交通大学 | Grain conveying device |
| CN202670742U (en) * | 2012-06-29 | 2013-01-16 | 爱思开实业（汕头）聚苯树脂有限公司 | Device for delivering solid powdery material |
| CN104132006A (en) * | 2014-08-07 | 2014-11-05 | 苏州淮通电气有限公司 | Ejector for jet pump |
| CN205855391U (en) * | 2016-07-20 | 2017-01-04 | 苏州中材建设有限公司 | For the issuance of materials device that granular solid is air conveying |
-
2016
- 2016-07-20 CN CN201610573381.1A patent/CN105966921A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB903102A (en) * | 1959-06-23 | 1962-08-09 | Acme Ventilating Ltd | Improvements relating to pneumatic conveyors for loose materials |
| JPH08113369A (en) * | 1994-10-17 | 1996-05-07 | Shohei Senda | Granule supplying device |
| CN2353940Y (en) * | 1998-09-15 | 1999-12-15 | 郑德明 | Low-pressure pneumatic continuous delivery pump |
| CN201367259Y (en) * | 2009-02-25 | 2009-12-23 | 大连森雅能源环保设备有限公司 | Jet type material feeder, |
| CN201785043U (en) * | 2010-06-11 | 2011-04-06 | 西安交通大学 | Grain conveying device |
| CN202670742U (en) * | 2012-06-29 | 2013-01-16 | 爱思开实业（汕头）聚苯树脂有限公司 | Device for delivering solid powdery material |
| CN104132006A (en) * | 2014-08-07 | 2014-11-05 | 苏州淮通电气有限公司 | Ejector for jet pump |
| CN205855391U (en) * | 2016-07-20 | 2017-01-04 | 苏州中材建设有限公司 | For the issuance of materials device that granular solid is air conveying |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107352274A (en) * | 2017-08-25 | 2017-11-17 | 天津商业大学 | A kind of regulatable new induction Pneumatic conveyer of particle concentration |
| CN107416529A (en) * | 2017-09-08 | 2017-12-01 | 中国华能集团清洁能源技术研究院有限公司 | A kind of Contiuum type air conveyor |
| CN114148759A (en) * | 2021-12-30 | 2022-03-08 | 南京翔瑞智能装备技术有限公司 | Gas-powder conveying device without returning charge |
| CN114148759B (en) * | 2021-12-30 | 2024-03-15 | 南京翔瑞智能装备技术有限公司 | Gas-powder conveying device without returning charge |
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| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
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| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160928 |