CN205929066U - Device of high efficiency preparation clay magma - Google Patents
Device of high efficiency preparation clay magma Download PDFInfo
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- CN205929066U CN205929066U CN201620962232.XU CN201620962232U CN205929066U CN 205929066 U CN205929066 U CN 205929066U CN 201620962232 U CN201620962232 U CN 201620962232U CN 205929066 U CN205929066 U CN 205929066U
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- clay
- oleo stock
- high pressure
- liquid outlet
- slurry
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Abstract
The utility model discloses a device of high efficiency preparation clay magma, deposiing impurity removing mechanism, clay thick liquid including clay thick liquid preparation mechanism, clay thick liquid and mixing evenly mechanism and clay magma and store the mechanism, clay thick liquid preparation mechanism includes that the clay stacks mechanism, slush pump and high pressure nozzle for the slurrying, the feed liquor torrential flow body turn -on connection of the play liquid of slush pump end and high pressure nozzle slurrying for, the play liquid end of high pressure nozzle is established in the mechanism is stacked to the clay slurrying for, and play liquid end and the clay thick liquid that the mechanism is stacked to the clay deposits impurity removing mechanism's feed liquor torrential flow body turn -on connection, and the feed liquor torrential flow body turn -on connection of mechanism is mixed evenly to play liquid end and clay thick liquid that the clay thick liquid deposits impurity removing mechanism, the mechanism was mixed evenly to the clay thick liquid play liquid end and the feed liquor torrential flow of the clay magma storage mechanism turn -on connection that personally experiences sth. Part of the body. The utility model discloses can improve traditional clay magma and make the production efficiency of thick liquid technology, reduce and make the thick liquid cost, ensure the full stuff quality of clay magma.
Description
Technical field
The present invention relates to pre grouting from the surface field, particularly to a kind of device rapidly and efficiently preparing clay oleo stock and slurrying
Technique.
Background technology
Pre grouting from the surface technology is the important method of mine water management and stratum consolidation, refers in shaft deepening or work surface
Before propulsion, rig is utilized to drill injected hole in vertical surrounding or target zone from ground, to basement rock water-bearing stratum or broken crack
Band carries out slip casting.Comprehensive grouting technique is advanced, the widely used a kind of complex art of technique in Current terrestrial pre-pouring grout,
Carry out successful Application in up to a hundred collieries and non-coal mine process of construction.
But, with the continuous expansion of mining scale, mine shaft depth is also increasingly deeper, no matter colliery is also non-colliery
Mountain, the hydrological geological conditions of deep formation are more complicated, and the quantities of pre grouting from the surface construction is increasing, for example：Colliery water
Calm down to bore region limestone aquifer improvement project, iron mine ore body Grouting Curtain Engineering etc., the duration is nervous, the pulping of clay oleo stock
Intensity is very big, the pulping amount at least 6000m of every month3More than.
At present, the grout making technolgy of clay oleo stock is divided into two big class：Soaking and stirring pulping method and clay pulper pulping method, this
Both of which has the disadvantage that：
(1) the pulping inefficiency of clay oleo stock, soaking and stirring pulping method pulping every month amount is not more than 1500m3, clay
Pulper pulping method pulping every month amount is not more than 3500m3It is impossible to meet more massive Grouting engineering demand；(2) clay is former
In slurry pulping process, workman's usage quantity is more, number of workers 7～9 people/machine-team of soaking and stirring method, clay pulper pulping method
Number of workers 5～6 people/machine-team, construction cost is very big；(3) clay pulper pulping method is higher for the requirement of intact clay,
Sand content is not more than 3%, and otherwise, the abrasion for equipment is larger, has a strong impact on the service life of clay pulper, therefore, sticks
The scope of selecting material of soil is less；(4) the pulping operation of clay oleo stock is more complicated, and the waste of raw materials artificially causing is more serious, if
Standby maintenance rate is higher, and maintenance in substantially two days once, leads to pulping cost to increase.(5) the having bad luck and stack of intact clay
Require very high, occupied ground is very big, and social benefit is poor.
Utility model content
In view of this, this utility model is to provide a kind of device rapidly and efficiently preparing clay oleo stock and pulping process,
Improve the production efficiency of traditional clay oleo stock pulping process, reduce pulping cost it is ensured that the pulp quality of clay oleo stock.
For solving the above problems, this utility model adopts the following technical scheme that：A kind of clay oleo stock rapidly and efficiently prepared
Device, mixes well mechanism and clay oleo stock stocking mechanism including clay slurry preparing mechanism, clay slurry removing impurity by means of precipitation mechanism, clay slurry,
Described clay slurry preparing mechanism includes clay stacking mechanism, slush pump and slurrying high pressure nozzle；The liquid outlet of described slush pump
It is connected with the liquid feeding end fluid communication of described slurrying high pressure nozzle, the liquid outlet of described slurrying high pressure nozzle is located at described sticking
In mound laying mechanism, the liquid feeding end fluid communication of the liquid outlet of described clay stacking mechanism and described clay slurry removing impurity by means of precipitation mechanism
Connect, the liquid feeding end fluid communication that the liquid outlet of described clay slurry removing impurity by means of precipitation mechanism mixes well mechanism with described clay slurry is connected,
The liquid outlet that described clay slurry mixes well mechanism is connected with the liquid feeding end fluid communication of described clay oleo stock stocking mechanism.
The above-mentioned device rapidly and efficiently preparing clay oleo stock, described clay oleo stock stocking mechanism includes clay oleo stock storage slurry
Pond, described clay oleo stock pulp storage tank pool wall is high 2.5m, the cut-pff wall of thick 0.4m；The liquid feeding end of described clay oleo stock pulp storage tank with
The liquid outlet fluid communication that described clay slurry mixes well mechanism connects.
The above-mentioned device rapidly and efficiently preparing clay oleo stock, described clay slurry is mixed well mechanism and is included oleo stock pond, mixes well with height
Pressure nozzle uses Pulp pump with mixing well, and described oleo stock pond pool wall is high 2.5m, the cut-pff wall of thick 0.4m；Described mixing well is set with Pulp pump
In described oleo stock pond, described mixing well is connected with the liquid outlet fluid communication of Pulp pump with described mixing well with the liquid feeding end of high pressure nozzle
Connect, described mixing well is located in described oleo stock pond with the liquid outlet of high pressure nozzle；The liquid outlet of described clay slurry removing impurity by means of precipitation mechanism
It is connected with the liquid feeding end fluid communication in described oleo stock pond, the described liquid outlet mixing well Pulp pump and described clay oleo stock pulp storage tank
Liquid feeding end fluid communication connects.
The above-mentioned device rapidly and efficiently preparing clay oleo stock, described clay slurry removing impurity by means of precipitation mechanism includes sedimentation tank, precipitation
Except using mixedly Pulp pump and mud purifiers, described removing impurity by means of precipitation Pulp pump is located in described sedimentation tank, described sedimentation tank pool wall
Cut-pff wall for high 2.5m, thick 0.4m；The liquid outlet of described clay stacking mechanism and the liquid feeding end fluid communication of described sedimentation tank
Connect；The liquid outlet of described removing impurity by means of precipitation Pulp pump is connected with the liquid feeding end fluid communication of described mud purifiers, described mud
The liquid outlet of slurry clearing machine is connected with the liquid feeding end fluid communication in described oleo stock pond.
The above-mentioned device rapidly and efficiently preparing clay oleo stock, the liquid outlet of described clay stacking mechanism and described sedimentation tank
Liquid feeding end pass through mud chute fluid communication connect；It is provided with filter screen, described removing impurity by means of precipitation is used in the liquid feeding end of described sedimentation tank
The liquid feeding end of Pulp pump is provided with screen cover.
The above-mentioned device quickly preparing clay oleo stock, described clay stacking mechanism includes Tu Chang and mud barricade, described mud
Slurry barricade is antiseepage mud barricade, and described mud barricade is provided with the slurry discharging hole running through described mud barricade, in described slurry discharging hole
It is provided with filter screen；Described slurrying high pressure nozzle is located on the described mud barricade close on described slurry discharging hole and described slurrying high pressure
The liquid outlet of nozzle is located at the side of the described mud barricade near described Tu Chang；Clay heap is located in described soil field, and described
Clay heap is the annular clay heap of fan, and described mud barricade is located at the fan-shaped edge of fan-shaped clay heap.
The above-mentioned device rapidly and efficiently preparing clay oleo stock, described slurrying high pressure nozzle is conical nozzle, described taper
The taper of nozzle is 12 °～14 °.
The above-mentioned device rapidly and efficiently preparing clay oleo stock, the liquid outlet of described slurrying high pressure nozzle can be with described mud
Slurry barricade is freely swung up and down for fulcrum, the angle that the liquid outlet of described slurrying high pressure nozzle can swing up and down
For -45 °～+45 °, the angle that the liquid outlet of described slurrying high pressure nozzle can swing is -60 °～+60 °；Described slurrying
It is less than or equal to 5m with the horizontal range between the liquid outlet of high pressure nozzle and clay heap edge.
The beneficial effects of the utility model are：
1. the pulping efficiency of clay oleo stock is greatly improved, and every month is up to 15000m3The needs of above slip casting scale, with biography
System grout making technolgy is compared, and pulping efficiency improves more than 4 times.
2. pulping process flow process is simple, and the scope of selecting material for intact clay is more extensive, plasticity index 10～17%, contains
The clay that sand amount is not more than 5% is all applicable.
3., in clay oleo stock pulping process, reduce workman's usage quantity, number of workers 2～3 people/machine-team, with traditional pulping
Technology is compared, and workman's labor service expenditure decreases about half, reduces the impact to pulp quality for the anthropic factor.
4. reduce the maintenance rate of slurry producing facility, main slurry producing facility keeps in repair 1 time for substantially every 7 days, has saved plant equipment
Maintenance cost.
5. improve the utilization rate of intact clay it is ensured that the pulp quality of clay oleo stock.
Brief description
Fig. 1 rapidly and efficiently prepares the structural representation of the device of clay oleo stock for this utility model；
Fig. 2 rapidly and efficiently prepares the structural representation of the slurrying high pressure nozzle in the device of clay oleo stock for this utility model
Figure；
Fig. 3 is the process schematic representation preparing clay oleo stock using the device rapidly and efficiently preparing clay oleo stock.
In figure：1- Tu Chang；2- mud barricade；3- slurrying high pressure nozzle；4- slush pump；5- filter screen；6- mud chute；7-
Sedimentation tank；8- removing impurity by means of precipitation Pulp pump；9- mud purifiers；10- oleo stock pond；11- mixes well and uses high pressure nozzle；12- mixes well use
Pulp pump；13- tee T；14- pulp storage tank；The liquid outlet of 15- slurrying high pressure nozzle.
Specific embodiment
For the scheme in clear explanation this utility model, preferred embodiment is given below and is described with reference to the accompanying drawings.
As shown in figure 1, this utility model rapidly and efficiently prepares the device of clay oleo stock, including clay slurry preparing mechanism, stick
Mechanism and clay oleo stock stocking mechanism are mixed well by soil paste removing impurity by means of precipitation mechanism, clay slurry.
Wherein, as shown in figure 1, described clay slurry preparing mechanism includes clay stacking mechanism, slush pump 4 and slurrying high pressure
Nozzle 3, described clay stacking mechanism includes Tu Chang and mud barricade 2, and described mud barricade 2 is antiseepage mud barricade 2, and described
Mud barricade 2 is provided with the slurry discharging hole running through described mud barricade 2, and is provided with filter screen 5 in described slurry discharging hole, and described slurry discharging hole is
Wide height is the square opening of 50cm, described slurrying high pressure nozzle 3 be located on the described mud barricade 2 close on described slurry discharging hole and
Described slurrying is located at the side of the described mud barricade 2 near described Tu Chang, wherein said slurrying with the liquid outlet of high pressure nozzle 3
Setting up point with high pressure nozzle 3 is 1.3m away from ground level, and the seamless steel pipe length for setting up described slurrying high pressure nozzle 3 is
2m, and described slurrying can carry out freely putting up and down with described mud barricade 2 for fulcrum with the liquid outlet of high pressure nozzle 3
Dynamic, the angle that the liquid outlet of described slurrying high pressure nozzle 3 can swing up and down is -45 °～+45 °, described slurrying high pressure nozzle
The angle that 3 liquid outlet can swing is -60 °～+60 °, and clay heap is located in described soil field, and described clay heap is
The annular clay heap of fan, described mud barricade 2 is located at the fan-shaped edge of fan-shaped clay heap, and described slurrying high pressure nozzle 3
Horizontal range between liquid outlet and clay heap is less than or equal to 5m.The slurrying high pressure nozzle selected in the present embodiment is taper
Nozzle, and the material of described conic nozzle is G105, a diameter of 30～35mm, and 12 ° of the nozzle taper of described conical nozzle
～14 °, as shown in Fig. 2 and the wall thickness of described conical nozzle is more than or equal to 5mm, and the described mud used in the present embodiment
Stock pump 4 is piston mud pump, and its technical parameter is：Piston diameter is 110mm, and nominal flow rate is 11L/s, and nominal pressure is
10MPa, suction caliber is 200mm, and discharge caliber is 75mm, and described slurrying high pressure nozzle 3 is Handheld high-voltage nozzle, described
Slush pump 4 is 3NB-260 slush pump, described and described mud barricade 2 high 1m, thick 0.28m, long 10m.
Described clay slurry removing impurity by means of precipitation mechanism includes sedimentation tank 7, removing impurity by means of precipitation Pulp pump 8 and mud purifiers 9, such as schemes
Shown in 1, described removing impurity by means of precipitation Pulp pump 8 is located in described sedimentation tank 7, and is provided with filter screen in the liquid feeding end of described sedimentation tank 7
5, and the liquid feeding end of described removing impurity by means of precipitation Pulp pump 8 is provided with screen cover, and in the present embodiment, described sedimentation tank 7 pool wall is height
2.5m, the cut-pff wall of thick 0.4m, a diameter of 6m of described sedimentation tank 7, described mud purifiers 9 are JSN-2C mud purifiers.
Described clay slurry is mixed well mechanism and is included oleo stock pond 10, mixes well with high pressure nozzle 11 and mix well with Pulp pump 12, described
Mix well and be located in described oleo stock pond 10 with Pulp pump 12, described mixing well uses slurry with the liquid feeding end of high pressure nozzle 11 with described mixing well
The liquid outlet of pump 12 passes through tee T 13 fluid communication and connects, and described mixing well is located at described oleo stock with the liquid outlet of high pressure nozzle 11
In pond 10, in the present embodiment, described oleo stock pond 10 pool wall is high 2.5m, the cut-pff wall of thick 0.4m, the diameter in described oleo stock pond 10
For 16m.
Described clay oleo stock stocking mechanism includes clay oleo stock pulp storage tank 14, as shown in figure 1, described clay oleo stock pulp storage tank
14 pool walls are high 2.5m, the cut-pff wall of thick 0.4m, a diameter of 16m of described clay oleo stock pulp storage tank 14.
Described removing impurity by means of precipitation Pulp pump 8 and described mixing well all are more than or equal to 13L/s's from flow with Pulp pump 12
Pulp pump, in the present embodiment, described Pulp pump is 80SZL-36 slag slurry pump under liquid.
In the described device rapidly and efficiently preparing clay oleo stock, as shown in figure 1, described Tu Chang pass through described slurry discharging hole with
And mud chute 6 is connected with the liquid feeding end fluid communication of described sedimentation tank 7, described removing impurity by means of precipitation Pulp pump 8 is located at described heavy
In shallow lake pond 7, described removing impurity by means of precipitation is connected with the liquid feeding end fluid communication of described mud purifiers 9 with the liquid outlet of Pulp pump 8, institute
The liquid outlet stating mud purifiers 9 is connected with the liquid feeding end fluid communication in described oleo stock pond 10, and described mixing well is set with Pulp pump 12
In described oleo stock pond 10, the described liquid outlet liquid feeding end with described clay oleo stock pulp storage tank 14 respectively mixed well with Pulp pump 12
Connected with the liquid feeding end fluid communication of high pressure nozzle 11 with described mixing well.
Prepare the pulping process of clay oleo stock using the described device rapidly and efficiently preparing clay oleo stock as shown in figure 3, wrapping
Include following steps：
(1) prepare clay one-level slurry using clay slurry preparing mechanism：Piston mud pump 4 and handss using high pressure big pump amount
The high-pressure injection current holding the generation of formula high pressure nozzle carry out broken cutting to the intact clay piled up, and generate clay one-level slurry, its
In, intact clay is original state sandy loam between 10%～17% for the plasticity index, and content is or not sticking grain (particle diameter is less than 0.005mm)
Less than 25%, sand content is not more than 5%, and content of organics is not more than 3%, and intact clay is piled up in described soil field, in sector
Pile up；The clay one-level slurry generating flows in described sedimentation tank 7 through described slurry discharging hole and described mud chute 6；
(2) clay prepared in step (1) one-level slurry clay slurry removing impurity by means of precipitation mechanism is carried out removing impurity by means of precipitation to obtain
Two grades of slurries of clay：The clay one-level prepared in step (1) is starched in described sedimentation tank 7 through described removing impurity by means of precipitation slurry
Pump 8 remove impurity processes and is transformed to two grades of slurries of clay；
(3) two grades of slurry clay slurry removing impurity by means of precipitation mechanisms of clay that step (2) is prepared are carried out desanding and obtain clay three
Level slurry：Two grades of slurries of the clay that step (2) is prepared pump into described mud purifiers 9 by described removing impurity by means of precipitation with Pulp pump 8 to be carried out
Desanding is processed, and after described mud purifiers 9 desanding is processed, two grades of slurries of clay become clay three-level slurry, wherein said mud
The disposal ability of slurry clearing machine 9 is more than or equal to 100m3/h；
(4) the clay three-level slurry clay slurry that step (3) is prepared is mixed well mechanism carry out mixing well process and obtain clay four
Level slurry：After clay three-level is starched and flowed in described oleo stock pond 10, high pressure is used with Pulp pump 12 and described mixing well by described mixing well
Nozzle 11 makes clay three-level slurry be stirred in described oleo stock pond 10, even if entering the clay three-level in described oleo stock pond 10
Slurry carries out interior circulation in described oleo stock pond 10, so that the locally inconsistent situation of the proportion of original clay three-level slurry, viscosity
Disappear so that the locally inconsistent clay three-level slurry of proportion, viscosity is changed into the clay level Four slurry of proportion, viscous consistency；This step
In rapid, in described oleo stock pond 10, the interior circulation of clay three-level slurry is periodically to carry out, continuously twice interval between interior circulation when
Between be less than or equal to 4 hours；Described interior circulation implementation is：Mix well mixing well in mechanism with clay slurry will be sticked with Pulp pump 12
The clay three-level stock pump that soil paste is mixed well in the oleo stock pond 10 in mechanism enters clay slurry to be mixed well and mixes well with high pressure nozzle 11 in mechanism,
Then via mix well with high pressure nozzle 11 by clay three-level slurry spray in oleo stock pond 10, through repetitious circulation it is ensured that slurry
Liquid reaches more preferable suspension, reduces the syneresis rate of serosity；
(5) the clay level Four stock pump that step (4) is prepared is entered storage in clay slurry stocking mechanism：In clay level Four slurry
Proportion reaches 1.13～1.25g/cm3, geneva viscosity reaches 16～23s, using described mix well be transported to Pulp pump 12 described
In pulp storage tank 14, you can obtain the clay oleo stock that can use；Clay oleo stock in described pulp storage tank 14 answers measurement in 4 hours once
Slurry viscosity and proportion.
In the present embodiment, described sedimentation tank 7, described oleo stock pond 10, described pulp storage tank 14 should periodically carry out clear basic skill or training's work, often
Conveying 600m3Clay oleo stock is cleared up once.
Above-described embodiment is only intended to clearly illustrate the invention example, and not the invention is had
The restriction of body embodiment.For those of ordinary skill in the field, can also make on the basis of the above description
The change of other multi-forms or variation.There is no need to be exhaustive to all of embodiment.All new in this practicality
Any obvious change extended out within the spirit of type and principle or variation are still in the invention claim
Protection domain among.
Claims (8)
1. a kind of device rapidly and efficiently preparing clay oleo stock is it is characterised in that include clay slurry preparing mechanism, clay slurry precipitation
Impurity removal mechanism, clay slurry mix well mechanism and clay oleo stock stocking mechanism, described clay slurry preparing mechanism include clay stacking mechanism,
Slush pump (4) and slurrying are with high pressure nozzle (3)；The liquid outlet of described slush pump (4) is entered with described slurrying high pressure nozzle (3)
Liquid end fluid communication connects, and the liquid outlet of described slurrying high pressure nozzle (3) is located in described clay stacking mechanism, described clay
The liquid outlet of stacking mechanism is connected with the liquid feeding end fluid communication of described clay slurry removing impurity by means of precipitation mechanism, and described clay slurry precipitation is removed
The liquid feeding end fluid communication that the liquid outlet of miscellaneous mechanism mixes well mechanism with described clay slurry is connected, and described clay slurry mixes well going out of mechanism
Liquid end is connected with the liquid feeding end fluid communication of described clay oleo stock stocking mechanism.
2. the device rapidly and efficiently preparing clay oleo stock according to claim 1 is it is characterised in that described clay oleo stock is stored up
Deposit mechanism and include clay oleo stock pulp storage tank (14), described clay oleo stock pulp storage tank (14) pool wall is high 2.5m, the antiseepage of thick 0.4m
Wall；The liquid outlet fluid communication that the liquid feeding end of described clay oleo stock pulp storage tank (14) mixes well mechanism with described clay slurry is connected.
3. the device rapidly and efficiently preparing clay oleo stock according to claim 2 is it is characterised in that described clay slurry is mixed well
Mechanism includes oleo stock pond (10), mixes well with high pressure nozzle (11) and mix well with Pulp pump (12), and described oleo stock pond (10) pool wall is
High 2.5m, the cut-pff wall of thick 0.4m；Described mixing well is located in described oleo stock pond (10) with Pulp pump (12), and described mixing well uses high pressure
The liquid feeding end of nozzle (11) is connected with the liquid outlet fluid communication of Pulp pump (12) with described mixing well, and described mixing well uses high pressure nozzle
(11) liquid outlet is located in described oleo stock pond (10)；The liquid outlet of described clay slurry removing impurity by means of precipitation mechanism and described oleo stock pond
(10) liquid feeding end fluid communication connects, the feed liquor of the described liquid outlet mixing well Pulp pump and described clay oleo stock pulp storage tank (14)
End fluid communication connects.
4. the device rapidly and efficiently preparing clay oleo stock according to claim 3 is it is characterised in that described clay slurry precipitates
Impurity removal mechanism includes sedimentation tank (7), removing impurity by means of precipitation Pulp pump (8) and mud purifiers (9), described removing impurity by means of precipitation Pulp pump
(8) it is located in described sedimentation tank (7), described sedimentation tank (7) pool wall is high 2.5m, the cut-pff wall of thick 0.4m；Described clay is stacked
The liquid outlet of mechanism is connected with the liquid feeding end fluid communication of described sedimentation tank (7)；Described removing impurity by means of precipitation Pulp pump (8) go out liquid
End is connected with the liquid feeding end fluid communication of described mud purifiers (9), the liquid outlet of described mud purifiers (9) and described oleo stock
The liquid feeding end fluid communication in pond (10) connects.
5. the device rapidly and efficiently preparing clay oleo stock according to claim 4 is it is characterised in that described clay stacks machine
The liquid outlet of structure is connected by mud chute (6) fluid communication with the liquid feeding end of described sedimentation tank (7)；Described sedimentation tank (7)
It is provided with filter screen (5), the liquid feeding end of described removing impurity by means of precipitation Pulp pump (8) is provided with screen cover in liquid feeding end.
6. according to the arbitrary described device rapidly and efficiently preparing clay oleo stock of Claims 1 to 5 it is characterised in that described stick
Mound laying mechanism includes Tu Chang (1) and mud barricade (2), and described mud barricade (2) is antiseepage mud barricade (2), described mud
Barricade (2) is provided with the slurry discharging hole running through described mud barricade (2), is provided with filter screen (5) in described slurry discharging hole；Described slurrying is high
Pressure nozzle (3) be located at close on described slurry discharging hole described mud barricade (2) is upper and the liquid outlet of described slurrying high pressure nozzle (3)
It is located at the side of the described mud barricade (2) near described Tu Chang (1)；Clay heap is located in described Tu Chang (1), and described clay
Heap is the annular clay heap of fan, and described mud barricade (2) is located at the fan-shaped edge of fan-shaped clay heap.
7. the device rapidly and efficiently preparing clay oleo stock according to claim 6 is it is characterised in that described slurrying high pressure
Nozzle is conical nozzle, and the taper of described conical nozzle is 12 °～14 °.
8. the device rapidly and efficiently preparing clay oleo stock according to claim 7 is it is characterised in that described slurrying high pressure
The liquid outlet of nozzle (3) can be freely swung with described mud barricade (2) up and down for fulcrum, described slurrying high pressure
The angle that the liquid outlet of nozzle (3) can swing up and down is -45 °～+45 °, and the liquid outlet of described slurrying high pressure nozzle (3) can be left
The angle of right swing is -60 °～+60 °；Level between the liquid outlet of high pressure nozzle (3) and clay heap edge for the described slurrying
Distance is less than or equal to 5m.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620962232.XU CN205929066U (en) | 2016-08-26 | 2016-08-26 | Device of high efficiency preparation clay magma |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620962232.XU CN205929066U (en) | 2016-08-26 | 2016-08-26 | Device of high efficiency preparation clay magma |
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| Publication Number | Publication Date |
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| CN205929066U true CN205929066U (en) | 2017-02-08 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620962232.XU Withdrawn - After Issue CN205929066U (en) | 2016-08-26 | 2016-08-26 | Device of high efficiency preparation clay magma |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106113277A (en) * | 2016-08-26 | 2016-11-16 | 北京中煤矿山工程有限公司 | A kind of device rapidly and efficiently preparing clay oleo stock and pulping process |
-
2016
- 2016-08-26 CN CN201620962232.XU patent/CN205929066U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106113277A (en) * | 2016-08-26 | 2016-11-16 | 北京中煤矿山工程有限公司 | A kind of device rapidly and efficiently preparing clay oleo stock and pulping process |
| CN106113277B (en) * | 2016-08-26 | 2018-09-11 | 北京中煤矿山工程有限公司 | A kind of device and pulping process rapidly and efficiently preparing clay magma |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170208 Effective date of abandoning: 20180911 |