CN206587610U - It is a kind of to be used for the live mixing arrangement of barged-in fill and solidification intensifier - Google Patents
It is a kind of to be used for the live mixing arrangement of barged-in fill and solidification intensifier Download PDFInfo
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- CN206587610U CN206587610U CN201620854919.1U CN201620854919U CN206587610U CN 206587610 U CN206587610 U CN 206587610U CN 201620854919 U CN201620854919 U CN 201620854919U CN 206587610 U CN206587610 U CN 206587610U
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- barged
- fill
- mixing
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- chamber
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- Consolidation Of Soil By Introduction Of Solidifying Substances Into Soil (AREA)
Abstract
The utility model discloses a kind of for barged-in fill and the live mixing arrangement of solidification intensifier, the device includes the connector being sequentially connected, receiving chamber, mixing flash chamber, injector;Receiving chamber, mixing flash chamber, injector are round tube shape structure;Mixing flash chamber arrival end and the port of export of receiving chamber are by being welded to connect, and the diameter for receiving chamber outlet end is less than the arrival end of mixing flash chamber.The arrival end of mixing dilatation chamber outlet end and injector is by being welded to connect, and the diameter of mixing dilatation chamber outlet end is more than the arrival end of injector.Mix the tubular structure changed inside flash chamber for internal diameter.Mix flash chamber and curing agent charging aperture is provided with the tube wall of the first segment pipe after its arrival end.What the utility model was provided is used for the live mixing arrangement of barged-in fill and solidification intensifier, being sufficiently mixed of barged-in fill and solidification intensifier, rapid curing, the purpose for shortening processing time can be reached in hydraulic reclamation pipe outlet formation mixing, dilatation and injection composite effect.
Description
Technical field
The utility model is related to a kind of mixing arrangement, in particular it relates to a kind of showing for barged-in fill and solidification intensifier
Field mixing arrangement.
Background technology
With developing rapidly for marine cause, Scale Sea Reclamation Project constantly expands, it is necessary to which advanced fill out extra large technology to meet
Large-scale artificial epeirogenetic and hydraulic fill foundation engineering.A large amount of earth materials needed for dredged mud can be solved into embankment as fill material
Carry out source problem, but a large amount of dredged muds that can solve to produce due to harbour and developing and maintaining for navigation channel take up an area stacking and to sea
The ecological problems such as the severe contamination that foreign environment is produced.Practice finds that barged-in fill water content is big, low bearing capacity, brings follow-up ground
Base reprocesses problem.
Existing solidification barged-in fill technology, its structure is mostly complex, need to use large scale equipment, to site requirements compared with
Height, mixture homogeneity is poor, extremely inefficient.
In summary, for the defect of prior art, it is accordingly required in particular to mixed using barged-in fill with the scene of solidification intensifier
Device, the problem of to solve mentioned above.
Utility model content
The purpose of this utility model is to provide the live mixing arrangement of a kind of barged-in fill and solidification intensifier, in hydraulic reclamation pipeline
Port of export formation mixing, dilatation and injection composite effect, reach being sufficiently mixed of barged-in fill and solidification intensifier, rapid curing,
Shorten the purpose of processing time.
In order to achieve the above object, the utility model provides a kind of barged-in fill that is used for and mixed with the scene of solidification intensifier
Device, wherein, the device includes the connector being sequentially connected, receiving chamber, mixing flash chamber, injector;It is described receiving chamber, mixed
It is round tube shape structure to close flash chamber, injector.The device can effectively it is mixed hydraulically-filled soil and solidification intensifier, accelerate hydraulic reclamation
Soil and the mixing velocity of solidification intensifier, the addition of solidification intensifier is not required to large-scale equipment can complete, additionally can be with
Ensure the spouting velocity of barged-in fill.
Above-mentioned is used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, described mixing flash chamber, it enters
The port of export of mouth end and receiving chamber is welded to connect by connecting plate, and the diameter of the port of export of receiving chamber is less than entering for mixing flash chamber
Mouth end.Due to the change of the pipe diameter, mixing flash chamber can play dilatation, improve mixed effect.
Above-mentioned is used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, described mixing flash chamber, it goes out
The arrival end of mouth end and injector is welded to connect by connecting plate, and the diameter for mixing the port of export of flash chamber is more than entering for injector
Mouth end.Injector is compared with mixing flash chamber, and pipe diameter reduces reducing, produces jet effect, and can realize and mix again,
The pressure and flow velocity for keeping barged-in fill to be sprayed with solidification intensifier mixture.
Above-mentioned is used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, inside described mixing flash chamber
The tubular structure changed for internal diameter;The internal diameter for the first segment pipe that the arrival end of mixing flash chamber starts is more than second segment thereafter
The internal diameter of pipeline, by the tapered connection of internal diameter between the first segment pipe and the second segment pipe, its section constitutes truncated cone-shaped, second segment
Pipeline afterbody is to the ejiction opening that an internal diameter flaring is constituted between the port of export of mixing flash chamber, and its section also constitutes truncated cone-shaped.
The rifle formation of flash chamber internal-internal model gun is mixed, mixing material rotation mixing can be made.
Above-mentioned is used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, described mixing flash chamber is at it
The tube wall of the first segment pipe after arrival end is provided with curing agent charging aperture, and described curing agent charging aperture is with mixing flash chamber
Side wall it is vertical, the size of curing agent charging aperture is adapted with solidification intensifier conveyance conduit.
Above-mentioned is used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, at described curing agent charging aperture
Provided with regulation switch.Solidification intensifier addition can be controlled by adjusting switch, regulation solidification intensifier and hydraulic reclamation
The addition ratio of soil.
Above-mentioned is used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, at described curing agent charging aperture
It is additionally provided with pressure gauge or current meter.Solidification intensifier can be added flow speed data by pressure gauge or current meter, be not only convenient for control
The addition ratio of solidification intensifier and barged-in fill, also makes solidification intensifier add flow velocity and is not changed by the change of external condition.
Above-mentioned is used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, described connector is ring flange,
Its material, size are adapted with barged-in fill pipeline, are fixed by clip and screw nut with barged-in fill pipeline, and scene mixing is filled
Put and be connected with barged-in fill pipeline.
Above-mentioned is used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, described receiving chamber is barged-in fill
Transition before being mixed with solidification intensifier, it is included is connected between one or two segment pipes, two segment pipes by flange, two segment pipes
In first paragraph be the rubber hose being connected with connector.
It is above-mentioned to be used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, described injector comprising one or
Connected between two segment pipes, two segment pipes by flange.
Above-mentioned is used for the live mixing arrangement of barged-in fill and solidification intensifier, wherein, described live mixing arrangement is pressed
Order according to connector, receiving chamber, mixing flash chamber, injector is assembled, and connector is connected with the barged-in fill pipeline at scene, twisted
Screw nut on tight clip and ring flange;The curing agent charging aperture for mixing flash chamber is connected with solidification intensifier conveyance conduit
Connect, connect startup dredge pump and mixed again.In mixed process, it can be determined by the reading on observed pressure table or current meter
The spouting velocity of barged-in fill, according to the spouting velocity of barged-in fill, pressure and flow in the unit interval, it is determined that solidification intensifier mix
Enter speed, the addition ratio of solidification intensifier is controlled with this.The incorporation of solidification intensifier is opened by regulation in actual use
Pass is controlled.
What the utility model was provided, which is used for barged-in fill and the live mixing arrangement of solidification intensifier, has advantages below:
Live mixing arrangement of the present utility model, wherein connector, receiving chamber, mixing flash chamber, are passing through by main flow
Receiving chamber, which enters, produces pressure drop and the mixing of jet progress barged-in fill and solidification intensifier after mixing flash chamber, and expands in jet
Hold mixing section front portion access current meter and valve, solidification is strengthened according to the addition ratio of the flow velocity of main flow, and solidification intensifier
The penetrating speed of agent is regulated and controled, and barged-in fill is sufficiently mixed with solidification intensifier.Injector internal diameter of the pipeline reducing, diameter become
It is small, jet effect is produced, and mixed again, the pressure and flow velocity for keeping barged-in fill to be sprayed with solidification intensifier mixture.
It is final in hydraulic reclamation pipe outlet formation mixing, dilatation and injection composite effect, reach the abundant of barged-in fill and solidification intensifier
Mixing, rapid curing, the purpose for shortening processing time.
Brief description of the drawings
Fig. 1 is to be of the present utility model for barged-in fill and the structure of the embodiment 1 of the live mixing arrangement of solidification intensifier
Schematic diagram.
Fig. 2 is to be of the present utility model for barged-in fill and the structure of the embodiment 2 of the live mixing arrangement of solidification intensifier
Schematic diagram.
Fig. 3 is used for inside the mixing flash chamber of the live mixing arrangement of barged-in fill and solidification intensifier to be of the present utility model
Structural representation.
Embodiment
Embodiment of the present utility model is further described below in conjunction with accompanying drawing.
What the utility model was provided is used for the live mixing arrangement of barged-in fill and solidification intensifier, includes the company being sequentially connected
Connect device 1, receiving chamber 2, mixing flash chamber 3, injector 4.Receiving chamber 2, mixing flash chamber 3, injector 4 are round tube shape structure.
Live mixing arrangement is connected by connector 1 with barged-in fill pipeline.The connector 1 be ring flange, its material, size with
Barged-in fill pipeline is adapted, and is fixed by clip and screw nut with barged-in fill pipeline, by live mixing arrangement and barged-in fill pipe
Road is connected.
Receiving chamber 2 receives to enter the barged-in fill of live mixing arrangement from barged-in fill pipeline.The receiving chamber 2 is barged-in fill and solid
Change the transition before reinforcing agent mixing, it is included is connected between one or two segment pipes, two segment pipes by flange, in two segment pipes
First paragraph is the rubber hose 6 being connected with connector 1.
Mixing flash chamber 3 mixes barged-in fill with solidification intensifier.Mix the arrival end of flash chamber 3 and the outlet of receiving chamber 2
End is welded to connect by connecting plate 7, and the diameter of the port of export of receiving chamber 2 is less than the arrival end of mixing flash chamber 3.Due to the pipeline
The change of diameter, mixing flash chamber 3 can play dilatation, improve mixed effect.
The arrival end of the mixing port of export of flash chamber 3 and injector 4 is welded to connect by connecting plate 7, mixes going out for flash chamber 3
The diameter at mouth end is more than the arrival end of injector 4.Injector 4 is compared with mixing flash chamber 3, and pipe diameter reduces reducing, produces
Jet effect, and can realize and mix again, the pressure and flow velocity for keeping barged-in fill to be sprayed with solidification intensifier mixture.
Mix the tubular structure that the inside of flash chamber 3 changes for internal diameter;The first paragraph pipe that the arrival end of mixing flash chamber 3 starts
The internal diameter in road 8 is more than the internal diameter of the second segment pipe 9 thereafter, tapered by internal diameter between the first segment pipe 8 and the second segment pipe 9
Connection, its section constitutes and constitutes an internal diameter between truncated cone-shaped 10, the port of export of the afterbody of the second segment pipe 9 to mixing flash chamber 3
The ejiction opening 11 of flaring, its section also constitutes truncated cone-shaped.The rifle formation of the internal-internal model gun of flash chamber 3 is mixed, can make to mix
Condensation material rotation mixing.
Mix flash chamber 3 and curing agent charging aperture 5, solidification are provided with the tube wall of the first segment pipe 8 after its arrival end
Agent charging aperture 5 is vertical with the side wall for mixing flash chamber 3.The size of curing agent charging aperture 5 is mutually fitted with solidification intensifier conveyance conduit
Match somebody with somebody.
Provided with regulation switch at curing agent charging aperture 5, pressure gauge or current meter are additionally provided with.Can be to solid by adjusting switch
Change reinforcing agent addition to be controlled, the addition ratio of regulation solidification intensifier and barged-in fill.Pressure gauge or current meter will can solidify
Reinforcing agent adds flow speed data, is not only convenient for controlling the addition ratio of solidification intensifier and barged-in fill, also adds solidification intensifier
Enter flow velocity by the change of external condition not changed.
Injector 4 is the outlet section of barged-in fill and solidification intensifier mixture.The injector 4 includes one or two segment pipes,
Connected between two segment pipes by flange.
What the utility model was provided is used for the live mixing arrangement of barged-in fill and solidification intensifier, according to connector 1, receives
Room 2, mixing flash chamber 3, injector 4 order assembling, by connector 1 with scene barged-in fill pipeline be connected, tighten clip with
Screw nut on ring flange;The curing agent charging aperture 5 for mixing flash chamber 3 is connected with solidification intensifier conveyance conduit, connect
The logical dredge pump that starts is mixed again.In mixed process, hydraulic reclamation can be determined by the reading on observed pressure table or current meter
Soil spouting velocity, according to the spouting velocity of barged-in fill, pressure and flow in the unit interval, it is determined that solidification intensifier incorporation speed
Degree, the addition ratio of solidification intensifier is controlled with this.The incorporation of solidification intensifier in actual use by regulation switch into
Row control.The device can effectively mixed hydraulically-filled soil and solidification intensifier, accelerate the mixing speed of barged-in fill and solidification intensifier
Degree, the addition of solidification intensifier is not required to large-scale equipment can complete, and can additionally ensure the spouting velocity of barged-in fill.
Embodiment of the present utility model is described in detail by the following examples.
Embodiment 1
As shown in figure 1, this is used for the live mixing arrangement of barged-in fill and solidification intensifier, the connector being sequentially connected is included
1st, receiving chamber 2, mixing flash chamber 3, injector 4.Receiving chamber 2, mixing flash chamber 3, injector 4 are round tube shape structure.
Connector 1 is ring flange, and live mixing arrangement is connected with barged-in fill pipeline.
Receiving chamber 2 receives to enter the barged-in fill of live mixing arrangement from barged-in fill pipeline.The receiving chamber 2 includes two sections of pipes
Connected between road, two segment pipes by flange, the first paragraph in two segment pipes is the rubber hose 6 being connected with connector 1.
Mixing flash chamber 3 mixes barged-in fill with solidification intensifier.Mix the arrival end of flash chamber 3 and the outlet of receiving chamber 2
End is welded to connect by connecting plate 7, and the diameter of the port of export of receiving chamber 2 is less than the arrival end of mixing flash chamber 3.Mix flash chamber
The arrival end of 3 ports of export and injector 4 is welded to connect by connecting plate 7, and the diameter for mixing the port of export of flash chamber 3 is more than injection
The arrival end of device 4.
As shown in figure 3, the tubular structure that the inside of mixing flash chamber 3 changes for internal diameter;The arrival end of mixing flash chamber 3 starts
The internal diameter of the first segment pipe 8 be more than the internal diameter of the second segment pipe 9 thereafter, lead between the first segment pipe 8 and the second segment pipe 9
The tapered connection of internal diameter is crossed, its section constitutes structure between truncated cone-shaped 10, the port of export of the afterbody of the second segment pipe 9 to mixing flash chamber 3
Into the ejiction opening 11 of an internal diameter flaring, its section also constitutes truncated cone-shaped.Mix the rifling knot of the internal-internal model gun of flash chamber 3
Structure, can make mixing material rotation mixing.
Mix flash chamber 3 and curing agent charging aperture 5, solidification are provided with the tube wall of the first segment pipe 8 after its arrival end
Provided with regulation switch at agent charging aperture 5, pressure gauge or current meter are additionally provided with.
Injector 4 is a segment pipe, is the outlet section of barged-in fill and solidification intensifier mixture.
Embodiment 2
As shown in Fig. 2 this is used for the live mixing arrangement of barged-in fill and solidification intensifier, the connector being sequentially connected is included
1st, receiving chamber 2, mixing flash chamber 3, injector 4.Receiving chamber 2, mixing flash chamber 3, injector 4 are round tube shape structure.
Connector 1 is ring flange, and live mixing arrangement is connected with barged-in fill pipeline.
Receiving chamber 2 is a segment pipe, receives to enter the barged-in fill of live mixing arrangement from barged-in fill pipeline.
Mixing flash chamber 3 mixes barged-in fill with solidification intensifier.Mix the arrival end of flash chamber 3 and the outlet of receiving chamber 2
End is welded to connect by connecting plate 7, and the diameter of the port of export of receiving chamber 2 is less than the arrival end of mixing flash chamber 3.Mix flash chamber
The arrival end of 3 ports of export and injector 4 is welded to connect by connecting plate 7, and the diameter for mixing the port of export of flash chamber 3 is more than injection
The arrival end of device 4.
Mix the tubular structure that the inside of flash chamber 3 changes for internal diameter;The first paragraph pipe that the arrival end of mixing flash chamber 3 starts
The internal diameter in road 8 is more than the internal diameter of the second segment pipe 9 thereafter, tapered by internal diameter between the first segment pipe 8 and the second segment pipe 9
Connection, its section constitutes and constitutes an internal diameter between truncated cone-shaped 10, the port of export of the afterbody of the second segment pipe 9 to mixing flash chamber 3
The ejiction opening 11 of flaring, its section also constitutes truncated cone-shaped.The rifle formation of the internal-internal model gun of flash chamber 3 is mixed, can make to mix
Condensation material rotation mixing.
Mix flash chamber 3 and curing agent charging aperture 5, solidification are provided with the tube wall of the first segment pipe 8 after its arrival end
Provided with regulation switch at agent charging aperture 5, pressure gauge or current meter are additionally provided with.
Injector 4 is the outlet section of barged-in fill and solidification intensifier mixture, and it is included between two segment pipes, two segment pipes
Connected by flange.
The live mixing arrangement of barged-in fill and solidification intensifier is used for using embodiment 1 or embodiment 2, solidification increasing is carried out
Strong agent and the live mixed hydraulically-filled implementation of barged-in fill.Before engineering construction, by the various pieces of device according to connector 1, receiving
Room 2, mixing flash chamber 3, the order assembling of injector 4, are connected with the barged-in fill pipeline at scene, tighten on clip and ring flange
Screw nut;Solidification intensifier conveyance conduit is connected with mixing the solidification intensifier inlet pipeline of flash chamber 3;Connect and start
Dredge pump, you can carry out mixed hydraulically-filled.
The jet dilatation mixing section that connector 1, receiving chamber 2, mixing flash chamber 3 are constituted, using jet and the powder of expanding type
The structure type of body-liquid mixer.Jet dilatation mixing section plays powder-liquid mixing of the liquid of main flow and the powder of time stream
Effect.Kinetic force is converted into pressure energy by jet dilatation mixing section, and jet is produced and mixed in blender helical structure by main flow
Clutch dilatation produces pressure drop, in equipment, and mixed fluid pressure can play a kind of material suction another higher than time stream
Plant the effect of material;The mixing of material is realized, vacuumizes, convey and stirs.Ratio can be carried out in use according to actual conditions
On adjustment.
The injection mixing section that injector 4 is constituted, internal diameter of the pipeline reducing, diameter diminish, and make the fluid for entering injection mixing section
Produce pressure increase, continue to rotate and secondary mixing, strengthen mixed process, reach between fluid fine dispersion and be sufficiently mixed
Purpose.
The utility model uses relatively simple helical inner structure, the structure type of model gun rifling, and pipeline
The dilatation of reducing, pressurization, on the one hand can reach the purpose for mixing barged-in fill with solidification intensifier, on the other hand again not
As for making internal mixer blockage phenomenon.Internal structure scheme can be changed as the case may be in engineering practice, with up to
To more preferable mixed effect.
The utility model is solid using switch control by the way that the secondary stream of powder solidification intensifier is imported in the barged-in fill of main flow
Change reinforcing agent inflow velocity, while connecting pressure gauge or current meter at switch interface, flow velocity is observed and controlled.Penetrating
Dilatation mixing section front portion access current meter is flowed, solidification enhancing is mixed according to the addition ratio of the flow velocity of main flow and solidification intensifier
The speed of agent is regulated and controled.Play and quickly, uniformly mix solidification intensifier and to barged-in fill and solidification intensifier with barged-in fill
The effect of the control of ratio.
What the utility model was provided is used for the live mixing arrangement of barged-in fill and solidification intensifier, and its application method is:Will
The utility model is connected with original barged-in fill pipeline, and the ejection of barged-in fill is determined by the reading on observed pressure table or current meter
Speed, according to the spouting velocity of barged-in fill in the unit interval, it is determined that solidification intensifier incorporation speed, controlled with this solidification increase
The addition ratio of strong agent.The incorporation of solidification intensifier is controlled by initial approach to become a Buddhist believer in actual use.
What the utility model was provided is used for the live mixing arrangement of barged-in fill and solidification intensifier, and port sizes can be voluntarily
Regulation, is applicable to original barged-in fill pipeline of different configuration, does not change original barged-in fill transfer designs and construction equipment.Its
It is simple in construction, it is adapted to large-scale production, curing efficiency is high.For different engineerings, mixing for solidification intensifier can be voluntarily adjusted
Amount ratio.The utility model is mainly made up of pipeline and internal structure, and device volume is small, easy to disassemble and carrying, is being constructed
It can be sprayed in journey and fill out each hydraulic reclamation position.Device can realizing self disassembling, assembling, be easy to the cleaning of equipment and guarantor after the completion of engineering
Support.Except solidifying hydraulic fill foundation for barged-in fill, other association areas are applied also for, practical value is high.
Although content of the present utility model is discussed in detail by above preferred embodiment, but it should be appreciated that on
The description stated is not considered as to limitation of the present utility model.After those skilled in the art have read the above, for
A variety of modifications and substitutions of the present utility model all will be apparent.Therefore, protection domain of the present utility model should be by appended
Claim limit.
Claims (8)
1. it is a kind of for barged-in fill and the live mixing arrangement of solidification intensifier, it is characterised in that the device is included and is sequentially connected
Connector, receiving chamber, mixing flash chamber, injector;Described receiving chamber, mixing flash chamber, injector are circular tube shaped knot
Structure;
The port of export of described mixing flash chamber, its arrival end and receiving chamber by being welded to connect, the port of export of receiving chamber it is straight
Footpath is less than the arrival end of mixing flash chamber;
The arrival end of described mixing flash chamber, its port of export and injector mixes the port of export of flash chamber by being welded to connect
Diameter be more than injector arrival end.
2. as claimed in claim 1 for barged-in fill and the live mixing arrangement of solidification intensifier, it is characterised in that described
Mix the tubular structure changed inside flash chamber for internal diameter;The internal diameter for the first segment pipe that the arrival end of mixing flash chamber starts is big
In the internal diameter of the second segment pipe thereafter, pass through the tapered connection of internal diameter, its section structure between the first segment pipe and the second segment pipe
Into truncated cone-shaped, the ejiction opening of an internal diameter flaring is constituted between the port of export of the second segment pipe afterbody to mixing flash chamber, it is cutd open
Face also constitutes truncated cone-shaped.
3. as claimed in claim 2 for barged-in fill and the live mixing arrangement of solidification intensifier, it is characterised in that described
Mix flash chamber and curing agent charging aperture, described curing agent charging are provided with the tube wall of the first segment pipe after its arrival end
Mouth is vertical with mixing the side wall of flash chamber.
4. as claimed in claim 3 for barged-in fill and the live mixing arrangement of solidification intensifier, it is characterised in that described
Provided with regulation switch at curing agent charging aperture.
5. as claimed in claim 4 for barged-in fill and the live mixing arrangement of solidification intensifier, it is characterised in that described
Pressure gauge or current meter are additionally provided with curing agent charging aperture.
6. as claimed in claim 1 for barged-in fill and the live mixing arrangement of solidification intensifier, it is characterised in that described
Connector is ring flange, and its size is adapted with barged-in fill pipeline, is fixed by clip and screw nut with barged-in fill pipeline, will
Live mixing arrangement is connected with barged-in fill pipeline.
7. as claimed in claim 1 for barged-in fill and the live mixing arrangement of solidification intensifier, it is characterised in that described
Receiving chamber includes to be connected between one or two segment pipes, two segment pipes by flange, and the first paragraph in two segment pipes is and connector
The rubber hose of connection.
8. as claimed in claim 1 for barged-in fill and the live mixing arrangement of solidification intensifier, it is characterised in that described
Injector is included to be connected between one or two segment pipes, two segment pipes by flange.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620854919.1U CN206587610U (en) | 2016-08-09 | 2016-08-09 | It is a kind of to be used for the live mixing arrangement of barged-in fill and solidification intensifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620854919.1U CN206587610U (en) | 2016-08-09 | 2016-08-09 | It is a kind of to be used for the live mixing arrangement of barged-in fill and solidification intensifier |
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Publication Number | Publication Date |
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CN206587610U true CN206587610U (en) | 2017-10-27 |
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CN201620854919.1U Expired - Fee Related CN206587610U (en) | 2016-08-09 | 2016-08-09 | It is a kind of to be used for the live mixing arrangement of barged-in fill and solidification intensifier |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106076136A (en) * | 2016-08-09 | 2016-11-09 | 刘文白 | A kind of on-the-spot mixing arrangement for barged-in fill Yu solidification intensifier |
CN113041871A (en) * | 2021-04-22 | 2021-06-29 | 昆明有色冶金设计研究院股份公司 | Stirring-free multiphase mixing and distributing device |
CN113750748A (en) * | 2021-10-19 | 2021-12-07 | 中船黄埔文冲船舶有限公司 | Desulfurization system for ship tail gas |
CN115054932A (en) * | 2022-08-19 | 2022-09-16 | 矿冶科技集团有限公司 | Concentrated full-tailing solidification and stockpiling system and method for carrying out concentrated full-tailing solidification and stockpiling by using same |
-
2016
- 2016-08-09 CN CN201620854919.1U patent/CN206587610U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106076136A (en) * | 2016-08-09 | 2016-11-09 | 刘文白 | A kind of on-the-spot mixing arrangement for barged-in fill Yu solidification intensifier |
CN113041871A (en) * | 2021-04-22 | 2021-06-29 | 昆明有色冶金设计研究院股份公司 | Stirring-free multiphase mixing and distributing device |
CN113750748A (en) * | 2021-10-19 | 2021-12-07 | 中船黄埔文冲船舶有限公司 | Desulfurization system for ship tail gas |
CN115054932A (en) * | 2022-08-19 | 2022-09-16 | 矿冶科技集团有限公司 | Concentrated full-tailing solidification and stockpiling system and method for carrying out concentrated full-tailing solidification and stockpiling by using same |
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