CN109056867A - A kind of high-pressure pneumatic adds the suction sand energy conserving system pushed away - Google Patents

A kind of high-pressure pneumatic adds the suction sand energy conserving system pushed away Download PDF

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Publication number
CN109056867A
CN109056867A CN201811058203.0A CN201811058203A CN109056867A CN 109056867 A CN109056867 A CN 109056867A CN 201811058203 A CN201811058203 A CN 201811058203A CN 109056867 A CN109056867 A CN 109056867A
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CN
China
Prior art keywords
sandpipe
diffuser
energy conserving
conserving system
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
Application number
CN201811058203.0A
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Chinese (zh)
Inventor
高新明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hunan Jinrui Energy Technology Co Ltd
Original Assignee
Hunan Jinrui Energy Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hunan Jinrui Energy Technology Co Ltd filed Critical Hunan Jinrui Energy Technology Co Ltd
Priority to CN201811058203.0A priority Critical patent/CN109056867A/en
Publication of CN109056867A publication Critical patent/CN109056867A/en
Pending legal-status Critical Current

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Classifications

    • EFIXED CONSTRUCTIONS
    • E02HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
    • E02FDREDGING; SOIL-SHIFTING
    • E02F3/00Dredgers; Soil-shifting machines
    • E02F3/04Dredgers; Soil-shifting machines mechanically-driven
    • E02F3/88Dredgers; Soil-shifting machines mechanically-driven with arrangements acting by a sucking or forcing effect, e.g. suction dredgers
    • EFIXED CONSTRUCTIONS
    • E02HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
    • E02FDREDGING; SOIL-SHIFTING
    • E02F3/00Dredgers; Soil-shifting machines
    • E02F3/04Dredgers; Soil-shifting machines mechanically-driven
    • E02F3/88Dredgers; Soil-shifting machines mechanically-driven with arrangements acting by a sucking or forcing effect, e.g. suction dredgers
    • E02F3/90Component parts, e.g. arrangement or adaptation of pumps

Abstract

The invention discloses a kind of high-pressure pneumatics to add the suction sand energy conserving system pushed away, including jet element, vacuum chamber, sand-feeding tube, compressed pipe, diffuser, out sandpipe, pressure piping;The suction sand energy conserving system further includes Pneumatic conveyer, which is arranged on diffuser or out sandpipe, and the inside of sandpipe is connected to towards the outlet side for going out sandpipe and with diffuser or out for the puff prot of the Pneumatic conveyer.Suction sand energy conserving system of the invention is on the basis of original scheme avoids waterpower from hitting, Pneumatic conveyer is added on diffuser or out sandpipe, enter expansion work in pipeline by the pressure-air that Pneumatic conveyer exports, sand aqueous mixtures is pushed quickly to flow, to guarantee efficiency of shaking out.

Description

A kind of high-pressure pneumatic adds the suction sand energy conserving system pushed away
Technical field
The present invention relates to a kind of suction sand system, the suction sand energy conserving system pushed away is added more particularly to a kind of high-pressure pneumatic.
Background technique
Patent No. CN201520599277.0 discloses a kind of suction-type dredge and efficiently inhales sand energy conserving system, including spray nozzle part Part, sand-feeding tube, compressed pipe, diffuser, goes out sandpipe and pressure piping at vacuum chamber;The jet element be mounted in vacuum chamber and The outlet end of positive vacuum chamber, the input end of the jet element are docked in the outlet of jet element with pressure piping, the vacuum The outlet end of room is docked with one end of compressed pipe, and the other end of the compressed pipe is docked with the small end of diffuser, the diffuser Big end docked with sandpipe out, the sand-feeding tube is mounted on vacuum chamber and the center line of sand-feeding tube and the vacuum chamber are penetrated The angle for flowing direction is 30 °~35 °.It is by setting the angle of the center line of sand-feeding tube and the jet direction of vacuum chamber to 30 °~35 ° make the conjunction speed range of two fluids farthest under this angle, and reduction waterpower as far as possible hits loss, to mention The efficiency of high vacuum chamber system simultaneously reduces system vibration, improves the service life of system.However, in subsequent use process In, although leading portion vacuum chamber portion has overcome the influence of waterpower shock, it has been found that the sand water mixing of back segment gone out in sandpipe The object rate of outflow is not high, and sand aqueous mixtures are from a part of kinetic energy consumption after vacuum chamber after compressed pipe, diffuser, going out sandpipe etc. On the long and narrow pipeline of section.Therefore, in order to further increase efficiency of shaking out, it would be highly desirable to be further improved.
Summary of the invention
In order to solve the above technical problems, the object of the present invention is to provide a kind of height that can improve the back segment mixture rate of outflow It calms the anger suction sand energy conserving system that is dynamic plus pushing away.
The technical solution adopted by the present invention is that:
A kind of high-pressure pneumatic adds the suction sand energy conserving system pushed away, including jet element, vacuum chamber, sand-feeding tube, compressed pipe, diffusion Pipe goes out sandpipe and pressure piping;The suction sand energy conserving system further includes Pneumatic conveyer, and Pneumatic conveyer setting is being expanded On separate tube or out sandpipe, with diffuser or out, the inside of sandpipe is connected to the puff prot of the Pneumatic conveyer and direction goes out sandpipe Outlet side.
It further limits, the center line of the center line of the puff prot jet direction and out sandpipe is in same plane and angle It is 0 °~10 °.
Preferably, the center line of the center line of the puff prot jet direction and sandpipe out is in same plane and angle is 5 ° ~10 °.
Further, the Pneumatic conveyer is located at the joining place of diffuser with sandpipe out.
Another restriction, the center line of the center line of the puff prot jet direction and out sandpipe is not in same plane.
Further, the puff prot has multiple, and multiple puff prots are distributed on jet ring, the jet ring As the Pneumatic conveyer and diffuser or out connector between sandpipe.
Beneficial effects of the present invention: suction sand energy conserving system of the invention original scheme avoid waterpower hit on the basis of, Pneumatic conveyer is added on diffuser or out sandpipe, is entered by the pressure-air that Pneumatic conveyer exports swollen in pipeline Swollen acting pushes sand aqueous mixtures quickly to flow, to guarantee efficiency of shaking out.
Detailed description of the invention
A specific embodiment of the invention is described further with reference to the accompanying drawing.
Fig. 1 is suction sand energy conserving system structural schematic diagram of the invention;
Fig. 2 is Pneumatic conveyer scheme of installation of the invention;
Fig. 3 is jet ring front view of the invention;
Fig. 4 is jet ring sectional view of the invention.
Specific embodiment
As shown in Figure 1, adding the suction sand energy conserving system pushed away, including jet element 1, vacuum for a kind of high-pressure pneumatic of the invention Room 2, compressed pipe 4, diffuser 5, goes out sandpipe 6, pressure piping 7 at sand-feeding tube 3;Jet element is mounted in vacuum chamber 2 and spray nozzle part The outlet end of positive vacuum chamber 2, the input end of jet element are docked in the outlet of part with pressure piping 7, the outlet of the vacuum chamber 2 End docked with one end of compressed pipe 4, the other end of compressed pipe 4 is docked with the small end of diffuser 5, the big end of the diffuser 5 and Sandpipe 6 docks out, and sand-feeding tube 3 is mounted on vacuum chamber 2 and the jet direction of the center line of sand-feeding tube 3 and the vacuum chamber 2 Angle be 30 °~35 °;Preferably 33 ° of golden section angles keep the conjunction speed range of two fluids farthest using this angle, Reduce waterpower as far as possible and hit loss, to improve the efficiency of vacuum chamber system.
The main improvement of the technical program is that suction sand energy conserving system of the invention further includes Pneumatic conveyer 8, should Pneumatic conveyer 8 is arranged on diffuser 5 or out sandpipe 6, the puff prot 81 of the Pneumatic conveyer 8 and diffuser 5 or The inside connection of sandpipe 6 and direction go out the outlet side of sandpipe 6 out.On the basis of original scheme avoids waterpower from hitting, add Pneumatic conveyer is entered swollen in pipeline on diffuser 5 or out sandpipe 6 by the pressure-air that Pneumatic conveyer 8 exports Swollen acting pushes sand aqueous mixtures quickly to flow, to guarantee efficiency of shaking out.
As the first preferred embodiment of the technical program, the center line of 81 jet direction of puff prot with shake out The center line of pipe 6 is in same plane and angle is 0 °~10 °, so that sand aqueous mixtures are directly toward under the action of pressure-air Output flow.The center line of the center line of preferential 81 jet direction of puff prot and sandpipe 6 out is in same plane and angle is 5 °~10 °.Such as Fig. 2, Fig. 4.
In the installation position selection of Pneumatic conveyer 8, in addition to being installed on diffuser 5 or the out body portion of sandpipe 6, It is also an option that being installed on the joining place of diffuser 5 with sandpipe 6 out, as shown in Figure 1.
As the another embodiment of the technical program, the center line of 81 jet direction of puff prot can also be set For center line with sandpipe 6 out not in same plane, this setting can be that pressure-air acts on entire pipeline cross to the greatest extent Sand aqueous mixtures on section make the sand aqueous mixtures on entire cross-section of pipeline generate rotation, rotation so that being more uniformly stressed The benefit of the sand aqueous mixtures turned is first is that conveying speed can be improved, second is that can make sand water to the generation impact of entire cross-section of pipeline Mixture cannot ensure that the unimpeded of entire pipeline in the generation deposition and fouling on cross-section of pipeline.
In addition, in the present embodiment, the puff prot 81 have it is multiple, as shown in Figure 3, Figure 4, multiple puff prots 81 It is distributed on jet ring 82, the jet ring 82 company between sandpipe 6 as Pneumatic conveyer 8 and diffuser 5 or out Fitting guarantees that the pressure-air of puff prot 81 from diffuser 5 or out multiple positions output pressure-air of sandpipe 6 is surround, guarantees Pressure-air acting is uniform, stable and efficient.
Meanwhile this programme still retains former scheme pressure piping 7 (water pump water outlet pipeline) and the selection of 6 diameter of sandpipe out.
1, the selection of the diameter of pressure piping 7 (water pump water outlet pipeline):
Pressure piping diameter phi D1 is determined according to pump capacity, lift, keeps pump discharge minimum to 2 on-way resistance of vacuum chamber, Reduce unnecessary headloss, improves efficiency.
2, go out the selection of the diameter of sandpipe 6:
The selection of 6 diameter phi D2 of sandpipe out, with go out sand aqueous mixtures in sandpipe 6 flow velocity be greater than gravel subsidence velocity be Principle makes larger gravel be unlikely to the blocking sandpipe that sinks.Sand efficiency is sent in raising.
3, the selection of length of tube is compressed:
The selection of 4 length L2 of compressed pipe, pumping fluid is from jet element 1 with velocities Vp and from sand-feeding tube 3 with speed V2 suction After upper fluid passes through vacuum chamber 2 (suction chamber), two fluids is sufficiently mixed in compressed pipe 4 kinetic energy being fully converted into pressure energy It is extruded in compressed pipe 4 with speed Vt as principle, reduces unnecessary kinetic energy rejection, improve system effectiveness.
4, the selection of 5 diffusion angle of diffuser and length:
The diffusion angle θ of diffuser 5 is no more than 11 degree according to hydrodynamics for principle, and length L3 is wanted meeting angle It asks rear microcephaly's docking compressed pipe 4, major part to dock out sandpipe 6 and determine, prevents from reducing energy due to the excessive generation vortex of diffusion angle Loss improves vacuum chamber efficiency.
The course of work of the technical program is high pressure water P1 (pressure), V1 (speed) 35m/s-65m/s, is sprayed from nozzle, Negative pressure is formed in the Q chamber of vacuum chamber, speed is carried out in compressed pipe 4 with P2 (pressure), V2 (speed) from sand-feeding tube 3 by atmospheric pressure Neutralization, with the extrusion of Vt speed, pressure enters by the pressure-air of Pneumatic conveyer 8 with P4 (pressure), V4 (speed) Sandpipe 6 pushes sand aqueous mixtures to flow out sandpipe 6 out with P5 (pressure), V5 (speed) by pressure-air expansion working.
The above description is only a preferred embodiment of the present invention, and the present invention is not limited to above embodiment, as long as with Essentially identical means realize that the technical solution of the object of the invention belongs within protection scope of the present invention.

Claims (6)

1. a kind of high-pressure pneumatic adds the suction sand energy conserving system pushed away, including jet element (1), vacuum chamber (2), sand-feeding tube (3), compression It manages (4), diffuser (5), go out sandpipe (6) and pressure piping (7);The jet element (1) is mounted in vacuum chamber (2) and nozzle The outlet ends of positive vacuum chamber (2), the input end of the jet element (1) are docked in the outlet of component (1) with pressure piping (7), The outlet end of the vacuum chamber (2) is docked with one end of compressed pipe (4), the other end and diffuser (5) of the compressed pipe (4) Small end docking, the big end of the diffuser (5) docks with sandpipe out (6), the sand-feeding tube (3) be mounted on vacuum chamber (2) and The angle of the jet direction of the center line of sand-feeding tube (3) and the vacuum chamber (2) is 30 °~35 °;It is characterized by: described Inhaling sand energy conserving system further includes Pneumatic conveyer (8), and the diffuser (5) are arranged in the Pneumatic conveyer (8) Or on sandpipe (6) out, the puff prot (81) of the Pneumatic conveyer (8) and the diffuser (5) or described The inside connection for going out sandpipe (6) and towards it is described go out sandpipe (6) outlet side.
2. high-pressure pneumatic according to claim 1 adds the suction sand energy conserving system pushed away, it is characterised in that: the puff prot (81) The center line of jet direction and it is described go out sandpipe (6) center line is in same plane and angle is 0 °~10 °.
3. high-pressure pneumatic according to claim 2 adds the suction sand energy conserving system pushed away, it is characterised in that: the puff prot (81) The center line of jet direction and it is described go out sandpipe (6) center line is in same plane and angle is 5 °~10 °.
4. high-pressure pneumatic according to claim 1 or 2 adds the suction sand energy conserving system pushed away, it is characterised in that: the pneumatic transporting Device (8) are sent to be located at the diffuser (5) and the joining place for going out sandpipe (6).
5. high-pressure pneumatic according to claim 1 or 2 adds the suction sand energy conserving system pushed away, it is characterised in that: the puff prot (81) center line of jet direction and the center line for going out sandpipe (6) be not in same plane.
6. high-pressure pneumatic according to claim 1 or 2 adds the suction sand energy conserving system pushed away, it is characterised in that: the puff prot (81) have multiple, multiple puff prots (81) are distributed on jet ring (82), described in the jet ring (82) is used as Pneumatic conveyer (8) and the diffuser (5) or it is described go out sandpipe (6) between connector.
CN201811058203.0A 2018-09-11 2018-09-11 A kind of high-pressure pneumatic adds the suction sand energy conserving system pushed away Pending CN109056867A (en)

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CN201811058203.0A CN109056867A (en) 2018-09-11 2018-09-11 A kind of high-pressure pneumatic adds the suction sand energy conserving system pushed away

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CN201811058203.0A CN109056867A (en) 2018-09-11 2018-09-11 A kind of high-pressure pneumatic adds the suction sand energy conserving system pushed away

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109853652A (en) * 2019-01-28 2019-06-07 南华大学 A kind of mill tailings library waterpower, which takes, sands flat platform

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05138055A (en) * 1991-11-12 1993-06-01 Canon Inc Impact type air grinder
JPH08155346A (en) * 1994-12-06 1996-06-18 Nordson Kk Accelerated air blower for electrostatic powder coating
JP2602386B2 (en) * 1992-02-12 1997-04-23 株式会社エヌ、アイ、テイ Slime suction hardener injection device
JP2006045836A (en) * 2004-08-03 2006-02-16 Takku:Kk Slime sucking and hardening material injecting method and device
CN203140198U (en) * 2013-04-02 2013-08-21 湖南有色重型机器有限责任公司 Spraying head
KR20140043425A (en) * 2014-03-20 2014-04-09 김용기 Dredging and dredged soil transfer apparatus and methods with high pressure water pumps and attractive force generators and vortex generators and air compressors
CN103938669A (en) * 2014-05-17 2014-07-23 安徽水利开发股份有限公司 Relief well dredging device
CN204826024U (en) * 2015-08-11 2015-12-02 长沙金佳机电设备有限公司 Sand economizer system is inhaled to suction -type dredge high efficiency

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05138055A (en) * 1991-11-12 1993-06-01 Canon Inc Impact type air grinder
JP2602386B2 (en) * 1992-02-12 1997-04-23 株式会社エヌ、アイ、テイ Slime suction hardener injection device
JPH08155346A (en) * 1994-12-06 1996-06-18 Nordson Kk Accelerated air blower for electrostatic powder coating
JP2006045836A (en) * 2004-08-03 2006-02-16 Takku:Kk Slime sucking and hardening material injecting method and device
CN203140198U (en) * 2013-04-02 2013-08-21 湖南有色重型机器有限责任公司 Spraying head
KR20140043425A (en) * 2014-03-20 2014-04-09 김용기 Dredging and dredged soil transfer apparatus and methods with high pressure water pumps and attractive force generators and vortex generators and air compressors
CN103938669A (en) * 2014-05-17 2014-07-23 安徽水利开发股份有限公司 Relief well dredging device
CN204826024U (en) * 2015-08-11 2015-12-02 长沙金佳机电设备有限公司 Sand economizer system is inhaled to suction -type dredge high efficiency

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109853652A (en) * 2019-01-28 2019-06-07 南华大学 A kind of mill tailings library waterpower, which takes, sands flat platform
CN109853652B (en) * 2019-01-28 2020-05-08 南华大学 Hydraulic sand taking platform for mine tailing pond

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