CN208035013U - Automatic mixing pulping system - Google Patents
Automatic mixing pulping system Download PDFInfo
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- CN208035013U CN208035013U CN201820253161.5U CN201820253161U CN208035013U CN 208035013 U CN208035013 U CN 208035013U CN 201820253161 U CN201820253161 U CN 201820253161U CN 208035013 U CN208035013 U CN 208035013U
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Abstract
Automatic mixing pulping system provided by the utility model, including slurry-storing box and powder material warehouse, the discharge port of powder material warehouse is equipped with weighing device, the discharge port of weighing device is connect directly or by conveying device with powder feeding warehouse, slurry-storing box is connected by the import of pipeline and delivery pump, the outlet of delivery pump and the import of mixer connect, and another import of mixer is connect with the outlet of powder feeding warehouse, and the outlet of mixer is connect by pipeline with slurry-storing box.By PLC control valves and delivery pump, the slurry extracted out from slurry-storing box passes through mixer, and inlet control valve is opened, and slurry-storing box is delivered to after the powder of powder feeding warehouse is mixed with slurry；So that powder after mixing, is closed circulation control valve with slurry, opens defeated slurry control valve and export slurry.By using charging of weighing, cooperation by negative pressure mixed feeding in the way of, avoids powder hardened, also improves the efficiency of entire slurrying using loop slurry, bentonite and polymer volume in slurry under reduction phase homogenous quantities.
Description
Technical field
The utility model is related to mud conditioning field, especially a kind of automatic mixing pulping system.
Background technology
In construction process, multigroup part of powder is needed to manufacture large capacity mixing slurry by certain ratio with water body
Body.Building-site at present, then a large amount of configurations are mixed and stirred by each component of manually weighing in slurry mixer, this by manually grasping
The pulping way disadvantage of work：Hand labor intensity is big；Metering cannot be accurate；Environment dust is big.
Chinese patent literature CN104989301A describes a kind of device that can prepare high quality mud automatically, including stirring
Bucket, feeding equipment and mud storage；Wherein, the feeding equipment include bentonite pulverizer, bentonite supply unit,
Na2CO3Conveyer, PHP conveying devices, conveyer belt and water tank；The bentonite supply unit, Na2CO3Conveyer and PHP
The discharge port of conveying device is provided with electric controlled regulating valve, and motor is provided with below the agitator, the output shaft of the motor with
Agitating shaft is sequentially connected；The discharge port of the bentonite pulverizer leads to bentonite supply unit, the bentonite by pipeline
Supply unit and Na2CO3The discharge port of conveyer is located at the top of conveyer belt, the discharge port of the PHP conveying devices and water tank
Agitator is led to by expects pipe；The agitator is connected to mud storage, the electric controlled regulating valve, motor, pressure sensing
Device and liquid level sensor are electrically connected with control unit.The utility model can continuous pulping, distributing precision height and stable quality.This is defeated
It send and matches mode and be easy to cause airborne dust, bentonite caking, and mixing efficiency is relatively low.
Chinese patent literature CN107443573A describes a kind of full-automatic mud mixing method, the 51st section of record of specification
PRIMARY STIRRING device is provided with the baiting structure of bushing type, but in this configuration, is affected by gravity, powder and slurries
Proportioning be difficult to reach more suitable ratio, be susceptible to bentonite knot grain, hardened phenomenon, to be uniformly mixed needs stir compared with
The long time.
To sum up all there is a problem of that pulping efficiency is relatively low in the prior art.
Invention content
The technical problem to be solved by the utility model is to provide a kind of automatic mixing pulping systems, can realize slurry
With the automatic mixing slurrying of powder, and pulping efficiency is higher, good mixing effect.
In order to solve the above technical problems, technical solution used by the utility model is：A kind of automatic mixing pulping system,
Including slurry-storing box and powder material warehouse, the discharge port of powder material warehouse is equipped with weighing device, the discharge port of weighing device directly or by
Conveying device is connect with powder feeding warehouse, and slurry-storing box is connected by the import of pipeline and delivery pump, the outlet of delivery pump with mix
The import of device connects, and another import of mixer is connect with the outlet of powder feeding warehouse, and the outlet of mixer passes through pipeline and storage
Starch case connection.
In preferred scheme, it is additionally provided with clarified water pump, clarified water pump is slurry-storing box feed flow by pipeline, and flow is equipped on pipeline
Meter and clear water automatic valve；
It is equipped with liquid level gauge and blender in slurry-storing box.
It is equipped in preferred scheme, between delivery pump and mixer into slurry control valve；
Conveying pump discharge is also connect by a pipeline with slurry-storing box, and circulation control valve is equipped on the pipeline.
In preferred scheme, the outlet of delivery pump is also with a piping connection, and the pipeline is equipped with defeated slurry control valve.
In preferred scheme, the outlet portion of powder feeding warehouse is equipped with inlet control valve.
In preferred scheme, the bottom of powder material warehouse is equipped with powder valve, and the lower section of powder valve is equipped with weighing cabin, on weighing cabin
Equipped with weighing sensor.
In preferred scheme, the conveying device is screw conveyor, the feed inlet of screw conveyor be equipped with cache into
Hopper；
It is equipped with chute in the discharge port of screw conveyor；
Weighing cabin is located at the top of caching feed hopper, and vibrating device is equipped in the conical lower portion side wall of weighing cabin.
In preferred scheme, in the mixer, jet pipe and shearing pipe are connect with negative pressure cavity, and negative pressure cavity is controlled with charging
The exit seal of valve connects, and the undergauge spout of jet pipe is inserted into the mixing mouth of shearing pipe, and the outer wall of undergauge spout with mix
The gap for charging is equipped between the inner wall of mouth；
The downstream for mixing mouth is equipped with shearing pipe reducing diameter part, and the downstream of shearing pipe reducing diameter part is equipped with shearing and manages expanding tapered portion.
A kind of automatic mixing pulping system provided by the utility model, by using charging of weighing, cooperation utilizes recycle slurry
Liquid avoids powder hardened in the way of negative pressure mixed feeding, also improves the efficiency of entire slurrying, reduces slurry under phase homogenous quantities
Middle bentonite and polymer volume.The system of the utility model uses hermetically sealed feeding manner, has prevented the dirt of dust completely
Dye.
Description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and examples：
Fig. 1 is the overall structure diagram of the utility model.
Fig. 2 is the schematic cross-sectional view of mixer in the utility model.
In figure：Expanding tapered portion 51 is managed in clarified water pump 1, liquid level gauge 2, slurry-storing box 3, clear water automatic valve 4, mixer 5, shearing,
Shearing pipe reducing diameter part 52, jet pipe 53, undergauge spout 54, negative pressure cavity 55, mixing mouth 56, powder feeding warehouse 6, inlet control valve 7, into
Starch control valve 8, circulation control valve 9, delivery pump 10, defeated slurry control valve 11, screw conveyor 12, weighing cabin 13, powder valve 14, title
Retransmit sensor 15, powder material warehouse 16, flowmeter 17, blender 18, bottom valve 19 of weighing, caching feed hopper 20, vibrating device 21.
Specific implementation mode
Embodiment 1：
In Fig. 1 ~ 2, a kind of automatic mixing pulping system, including slurry-storing box 3 and powder material warehouse 16, powder material warehouse 16 go out
Material mouth is equipped with weighing device, and the discharge port of weighing device is connect directly or by conveying device with powder feeding warehouse 6, slurry-storing box 3
Connect with the import of delivery pump 10 by pipeline, the outlet of delivery pump 10 is connect with the import of mixer 5, mixer 5 it is another
Import is connect with the outlet of powder feeding warehouse 6, and the outlet of mixer 5 is connect by pipeline with slurry-storing box 3.Thus structure passes through
The mode of loop slurry mixes powder, and recycle feed improves pulping efficiency.Delivery pump in this example includes shear pump, centrifugation
Pump, piston pump, diaphragm pump.
In preferred scheme such as Fig. 1, it is additionally provided with clarified water pump 1, clarified water pump 1 is 3 feed flow of slurry-storing box by pipeline, on pipeline
Equipped with flowmeter 17 and clear water automatic valve 4；
It is equipped with liquid level gauge 2 and blender 18 in slurry-storing box 3.Thus structure realizes automatic supply clear water.Clear water herein
Can be circular treatment water.
In preferred scheme such as Fig. 1, it is equipped between delivery pump 10 and mixer 5 into slurry control valve 8；
The outlet of delivery pump 10 is also connect by a pipeline with slurry-storing box 3, and circulation control valve 9 is equipped on the pipeline.By
This structure realizes the switching of charging and circulation stirring pattern by controlling into the keying of slurry control valve 8 and circulation control valve 9.
In preferred scheme, the outlet of delivery pump 10 is also with a piping connection, and the pipeline is equipped with defeated slurry control valve 11.
Thus structure controls plasma discharge.
In preferred scheme, the outlet portion of powder feeding warehouse 6 is equipped with inlet control valve 7.Thus structure, realization automatically control
Mixed feeding.
In preferred scheme such as Fig. 1, the bottom of powder material warehouse 16 is equipped with powder valve 14, and the powder valve 14 in this example uses star
Type rotary valve.The lower section of powder valve 14 is equipped with weighing cabin 13, and weighing cabin 13 is equipped with weighing sensor 15.Using suspension in this example
The scheme weighed closes bottom valve 19 of weighing in weighing process, stops discharge, to improve the accuracy weighed.
In preferred scheme, land weighting manner can also be used equipped with weighing sensor 15 in weighing cabin 13.
In preferred scheme, the conveying device is screw conveyor 12, it is preferred that the feed inlet of screw conveyor 12
Equipped with caching feed hopper 20；Thus structure, when weighing cabin 13 is in weighing process, caching feed hopper 20 can ensure that charging will not
It interrupts.
It is equipped with chute in the discharge port of screw conveyor 12；Thus structure reduces airborne dust.
Weighing cabin 13 is located at the top of caching feed hopper 20, and vibrating device is equipped in the conical lower portion side wall of weighing cabin 13
21.Thus structure realizes the quick discharge of weighing cabin 13.
In preferred scheme such as Fig. 2, in the mixer 5, jet pipe 53 and shearing are managed and are connect with negative pressure cavity 55, negative pressure cavity
55 connect with the exit seal of inlet control valve 7, and the undergauge spout 54 of jet pipe 53 is inserted into the mixing mouth 56 of shearing pipe, and is contracted
The gap for charging is equipped between the outer wall of diameter spout 54 and the inner wall for mixing mouth 56；
The downstream for mixing mouth 56 is equipped with shearing pipe reducing diameter part 52, and the downstream of shearing pipe reducing diameter part 52 is equipped with shearing pipe expanding prick
Shape portion 51.Thus structure is realized and generates negative pressure in negative pressure cavity 55, and mixing is realized to sweep along powder into shearing pipe, by
It is not influenced by gravitation in powder, mixing ratio can be preferably controlled in mixed process, avoided hardened and knot grain, improve slurrying effect
Rate.
Embodiment 2：
A kind of multigroup part of automatic mixing pulping process, mixer 5 is arranged below powder material warehouse 16, is made using delivery pump 10
Slurries recycle between mixer 5, pipeline and powder material warehouse 16, the negative pressure generated in mixer 5 using the flowing of slurries, real
Existing powder charging and the cycle mixing of slurries powder.
It is further preferred that a kind of multigroup part of automatic mixing pulping process, the discharge port of powder material warehouse 16 is equipped with dress of weighing
It sets, the discharge port of weighing device is connect by conveying device with powder feeding warehouse 6, and slurry-storing box 3 passes through pipeline and delivery pump 10
Import connects, and the outlet of delivery pump 10 is connect with the import of mixer 5, another import of mixer 5 and going out for powder feeding warehouse 6
Mouth connection, the outlet of mixer 5 is connect by pipeline with slurry-storing box 3；
It is equipped between delivery pump 10 and mixer 5 into slurry control valve 8；
The outlet of delivery pump 10 is also connect by a pipeline with slurry-storing box 3, and circulation control valve 9 is equipped on the pipeline；
The outlet of delivery pump 10 is also connect by a pipeline with slurry-storing box 3, and circulation control valve 9 is equipped on the pipeline；
Weighing device, conveying device, clear water automatic valve 4, inlet control valve 7, into slurry control valve 8, circulation control valve 9, defeated
Pump 10, defeated slurry control valve 11 is sent to be connect with PLC；
It is further comprising the steps of：
S1, conveying device are by the powder carry after weighing to powder feeding warehouse 6；
S2, PLC control defeated slurry control valve 11 and circulation control valve 9 is closed, and are opened into slurry control valve 8, and delivery pump 10 is run,
The slurry extracted out from slurry-storing box 3 passes through mixer 5, and slurry-storing box 3 is delivered to after the powder of powder feeding warehouse 6 is mixed with slurry；
S3, reach setting value when powder is fed, close into slurry control valve 8, ON cycle control valve 9, powder is made by cycle
Material is sufficiently mixed with slurry；
S4, after mixing closes circulation control valve 9, opens the defeated output of slurry control valve 11 slurry.
In preferred scheme, the powder material warehouse 16, weighing cabin 13, conveying device, powder feeding warehouse 6 and mixer 5
To be multigroup, a kind of every group of powder of correspondence；
Or only powder material warehouse 16, weighing cabin 13, conveying device, be a kind of multigroup, every group of powder of correspondence；
Powder is mixed with slurry using one or more delivery pump 10；
When being mixed using a delivery pump 10, being mixed into slurry control valve 8 for one of which, other groups are opened
Be turned off into slurry control valve 8 and circulation control valve 9, when the charging of this group of powder reaches setting value, close being controlled into slurry for the group
Valve 8, open in turn other each groups into slurry control valve 8.
When powder material warehouse 16, weighing cabin 13 and conveying device are multigroup, when powder feeding warehouse 6 is only with one, certain organizes powder
Body blending transportation in mixer 5 enters in slurry-storing box 3, after powder mixing delay, adds other groups of powders successively.
Embodiment 3：
Further the utility model is illustrated by taking optimum embodiment as an example referring to Fig. 1, clarified water pump 1, it is preferred to use
Centrifugal pump is connect by flowmeter 17 and clear water automatic valve 4 with slurry-storing box 3, for supplying clear water or recirculated water to slurry-storing box 3,
It is equipped with blender 18 in slurry-storing box 3, is additionally provided with liquid level gauge 2, it is preferred to use ultrasonic liquid level meter, preferred blender 18 is using upright
Driving structure on axis.It is directly connect by a hand-operated valve or with the import of delivery pump 10, delivery pump 10 in the side of slurry-storing box 3
It is preferred that using centrifugal pump, piston pump, shear pump or diaphragm pump.Further preferably use shear pump.The outlet of delivery pump 10 and three
Piping connection, a pipeline connect defeated slurry control valve 11 for plasma discharge；One connects slurry-storing box 3 by circulation control valve 9, for starching
Liquid recycles, and can fully be sheared to bentonite and polymer such as hydrolysed polyacrylic ammonium PHP, and mud property is improved,
Reduce bentonite and polymer volume；Another pipeline taps into slurry control valve 8 and mixer 5, for passing through slurries mixed powder
Charging.The outlet of mixer 5 is connect with slurry-storing box 3, another import for being located at top is connect with inlet control valve 7, charging control
Valve 7 processed is located at the bottom of powder feeding warehouse 6.Wherein mixer 5 is using such as the negative pressure feeding structure in Fig. 2, jet pipe 53 and shearing
Pipe is connect with negative pressure cavity 55, and the undergauge spout 54 of jet pipe 53 is socketed in the mixing mouth 56 of shearing pipe, and undergauge spout 54 is outer
The gap for charging is equipped between wall and the inner wall for mixing mouth 56；The downstream for mixing mouth 56 is equipped with shearing pipe reducing diameter part 52, cuts
The internal diameter of Pipe Cutting reducing diameter part 52 is more than the outer diameter of undergauge spout 54, and the downstream of shearing pipe reducing diameter part 52 is equipped with shearing and manages expanding taper
Portion 51.The big end internal diameter that expanding tapered portion 51 is managed in shearing is more than the outer diameter that other positions are managed in shearing.Thus structure, reduce because into
The impact that material strip comes.When slurries are pushed by delivery pump 10, it is injected in shearing pipe from undergauge spout 54, is generated in negative pressure cavity 55
Negative pressure makes slurries that part powder be swept along to enter in shearing pipe, and is sufficiently mixed, and thus improves pulping efficiency.When charging reaches
After proportioning, close into slurry control valve 8,9 further circulating pulp-making of ON cycle control valve.
According to construction site height, this example uses screw conveyor 12 to be fed for powder feeding warehouse 6, screw conveyor 12
Discharge port is equipped with rubber sliding cylinder, and the import of screw conveyor 12 is equipped with caching feed hopper 20, and 20 top of caching feed hopper, which is equipped with, to be claimed
Weight storehouse 13,13 top of weighing cabin are equipped with powder material warehouse 16, and the wherein bottom of weighing cabin 13 is equipped with bottom valve 19 of weighing, powder material warehouse 16
Bottom be equipped with star-like rotary valve, powder material warehouse 16, weighing cabin 13 is gentle deposit into hopper 20 between be designed with flexible dustproof shield
Cylinder, avoids dust from escaping.It is more to cache feed hopper 20, weighing cabin 13, screw conveyor 12, powder feeding warehouse 6 and mixer 5
Group, it is corresponding with dispensing respectively, such as bentonite and polymer and other dispensings.This example using the same delivery pump 10 into
It advances material, after the completion of feeding manner is a kind of charging of powder, then inputs in another powder to powder feeding warehouse 6, or use
Timesharing is fed, i.e., interval alternately inputs different powders.
Control device in this example uses PLC, flowmeter 17, liquid level gauge 2, weighing cabin 13 weighing sensor 15 and PLC
Input terminal electrical connection, clear water automatic valve 4, blender 18, inlet control valve 7, into slurry control valve 8, circulation control valve 9, conveying
The output end electricity of pump 10, defeated slurry control valve 11, screw conveyor 12, bottom valve 19 of weighing, vibrating device 21 and powder valve 14 and PLC
Connection.Multigroup feed, connection type is identical, no longer repeats one by one.
In use, being arranged as required to the proportioning of each auxiliary material in mud, PLC controls clarified water pump 1 and starts, and gives slurry-storing box 3
Recirculated water after middle injected clear water or processing, after liquid level gauge 2 detects the water inlet pipe certain altitude that clear water is more than delivery pump 10, PLC
Start delivery pump 10 and blender 18, after reaching preset value, PLC controls clarified water pump 1 and closes；Meanwhile PLC control powders valve 14 is opened
It opens, powder enters in weighing cabin 13, and after reaching constant weight, weight is fed back to PLC by weighing sensor 15, reaches default
Value, PLC control the unlatching of bottom valve 19 of weighing, and powder valve 14 is closed；Powder enters caching feed hopper 20, while vibrating device 21
Start, it is ensured that powder is completely exhausted out, and closes bottom valve 19 of weighing.It weighs and is zeroed again.Open powder valve 14.Meanwhile spiral transferring
Sending machine 12 to start will cache in the powder carry to powder feeding warehouse 6 in feed hopper 20.Inlet control valve 7 and into slurry control valve 8
It opens, circulation control valve 9 and defeated slurry control valve 11 are closed, and slurries enter in mixer 5, realize negative pressure charging.Weighing cabin 13
Feed weight and mixer 5 processing capacity as reference, and the opening time for calculating into slurry control valve 8 is used as with reference to controlling
Parameter, i.e., with the processing capacity X of mixer 5, units/kg/min and the opening time T into slurry control valve 81, as automatically controlling
Parameter coordinates the data on flows of delivery pump 10, controls the inlet amount of weighing cabin 13.To ensure that charging meets supply requirement, also want
Powder is avoided to overflow.Other powders also use identical control strategy.After the completion of a kind of charging of powder, it is then turned on another powder
The charging of material, or alternately input powder.After the completion of the charging of all powders, close into slurry control valve 8, ON cycle control valve 9,
Automatic-circulation milk-preparing.After reaching preset time, circulation control valve 9 is closed, defeated slurry control valve 11 is opened, conveys the mud prepared
To next procedure.
The above embodiments are only the optimal technical scheme of the utility model, and are not construed as the limit for the utility model
System, the technical solution that the scope of protection of the utility model should be recorded with claim include the technical solution of claim record
The equivalents of middle technical characteristic are protection domain.Equivalent replacement i.e. within this range is improved, also in the utility model
Protection domain within.
Claims (8)
1. a kind of automatic mixing pulping system, including slurry-storing box（3）And powder material warehouse（16）, powder material warehouse（16）Discharge port set
There is weighing device, it is characterized in that：The discharge port of weighing device is directly or by conveying device and powder feeding warehouse（6）Connection, storage
Starch case（3）Pass through pipeline and delivery pump（10）Import connection, delivery pump（10）Outlet and mixer（5）Import connection,
Mixer（5）Another import and powder feeding warehouse（6）Outlet connection, mixer（5）Outlet pass through pipeline and slurry-storing box
（3）Connection.
2. a kind of automatic mixing pulping system according to claim 1, it is characterized in that：It is additionally provided with clarified water pump（1）, clarified water pump
（1）It is slurry-storing box by pipeline（3）Feed flow is equipped with flowmeter on pipeline（17）With clear water automatic valve（4）；
In slurry-storing box（3）Equipped with liquid level gauge（2）And blender（18）.
3. a kind of automatic mixing pulping system according to claim 1, it is characterized in that：Delivery pump（10）With mixer（5）
Between be equipped with into slurry control valve（8）；
Delivery pump（10）Outlet also passes through a pipeline and slurry-storing box（3）Connection is equipped with circulation control valve on the pipeline（9）.
4. a kind of automatic mixing pulping system according to claim 1, it is characterized in that：Delivery pump（10）Outlet also with one
Piping connection, the pipeline are equipped with defeated slurry control valve（11）.
5. a kind of automatic mixing pulping system according to claim 1, it is characterized in that：Powder feeding warehouse（6）Outlet portion
Equipped with inlet control valve（7）.
6. a kind of automatic mixing pulping system according to claim 1, it is characterized in that：Powder material warehouse（16）Bottom be equipped with
Powder valve（14）, powder valve（14）Lower section be equipped with weighing cabin（13）, weighing cabin（13）It is equipped with weighing sensor（15）.
7. a kind of automatic mixing pulping system according to claim 6, it is characterized in that：The conveying device is spiral transferring
Send machine（12）, screw conveyor（12）Feed inlet be equipped with caching feed hopper（20）；
In screw conveyor（12）Discharge port be equipped with chute；
Weighing cabin（13）Positioned at caching feed hopper（20）Top, in weighing cabin（13）Conical lower portion side wall be equipped with vibrating device
（21）.
8. according to a kind of automatic mixing pulping system of claim 1 ~ 7 any one of them, it is characterized in that：The mixer
（5）In, jet pipe（53）With shearing pipe and negative pressure cavity（55）Connection, negative pressure cavity（55）With inlet control valve（7）Exit seal connect
It connects, jet pipe（53）Undergauge spout（54）It is inserted into the mixing mouth of shearing pipe（56）It is interior, and undergauge spout（54）Outer wall with it is mixed
It heals up（56）Inner wall between be equipped with for charging gap；
Mix mouth（56）Downstream be equipped with shearing pipe reducing diameter part（52）, shear pipe reducing diameter part（52）Downstream be equipped with shearing pipe it is expanding
Tapered portion（51）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820253161.5U CN208035013U (en) | 2018-02-12 | 2018-02-12 | Automatic mixing pulping system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820253161.5U CN208035013U (en) | 2018-02-12 | 2018-02-12 | Automatic mixing pulping system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208035013U true CN208035013U (en) | 2018-11-02 |
Family
ID=63953127
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820253161.5U Active CN208035013U (en) | 2018-02-12 | 2018-02-12 | Automatic mixing pulping system |
Country Status (1)
| Country | Link |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110142870A (en) * | 2018-02-12 | 2019-08-20 | 三川德青工程机械有限公司 | Automatic mixing pulping system and method |
| CN112157108A (en) * | 2020-09-09 | 2021-01-01 | 杭州灰弘环保科技有限公司 | Household garbage incineration fly ash pulping and washing device and pulping and washing method thereof |
| CN115256634A (en) * | 2022-07-22 | 2022-11-01 | 榆林学院 | Automatic proportioning and sampling device for slurry bentonite production line |
-
2018
- 2018-02-12 CN CN201820253161.5U patent/CN208035013U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110142870A (en) * | 2018-02-12 | 2019-08-20 | 三川德青工程机械有限公司 | Automatic mixing pulping system and method |
| CN112157108A (en) * | 2020-09-09 | 2021-01-01 | 杭州灰弘环保科技有限公司 | Household garbage incineration fly ash pulping and washing device and pulping and washing method thereof |
| CN115256634A (en) * | 2022-07-22 | 2022-11-01 | 榆林学院 | Automatic proportioning and sampling device for slurry bentonite production line |
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