CN106606949A - Filter cake slurrying device - Google Patents
Filter cake slurrying device Download PDFInfo
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- CN106606949A CN106606949A CN201510696472.XA CN201510696472A CN106606949A CN 106606949 A CN106606949 A CN 106606949A CN 201510696472 A CN201510696472 A CN 201510696472A CN 106606949 A CN106606949 A CN 106606949A
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- filter cake
- stirring paddle
- stirring
- sizing device
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Abstract
The invention discloses a filter cake slurrying device including a beating tank (1) and a strip extruder (2), wherein the beating tank (1) is internally provided with stirring impellers; the end port of an extruding material outlet (22) of the strip extruder is provided with a screen (3) and extends into a tank body (11); a filter cake added from a feed inlet can be extruded into a filter cake extruded strip by the strip extruder; the extruded strip is dispersed via the screen at the extruding material outlet and then is further dispersed in the tank body via the water shearing force action, to form slurry under stirring of the stirring impellers. The stirring impellers can comprise a helical internal stirring impeller (7) and cage-shaped external stirring impellers (8), and the external stirring impellers radially alternately sleeve the exterior of the internal stirring impeller; a stirring motor (4) can respectively independently drive the internal stirring impeller and the external stirring impellers so as to achieve vertically lifting and falling, and can drive homonymous rotation or reverse rotation of the internal stirring impeller and the external stirring impellers. The filter cake slurrying device can fully crush the filter cake, has the advantages of good stirring effect and high slurrying efficiency, and can effectively relieve blocking of the discharge port and bottom deposition of the beating tank.
Description
Technical field
The invention belongs to field of catalyst preparation, especially, is related to a kind of the efficient into slurry dress of high viscous filter cake
Put and its method.
Background technology
In the preparation process of catalyst, filter cake is generally needed into the often important process procedure of slurry, filter cake
To be sufficiently agitated to form serosity in hollander tub.
For example, ZL201320342061.7 discloses a kind of white carbon filter cake hollander tub (or claiming beating tank),
Including cell body, Power Drive Unit and pump, shaft is installed in cell body, shaft is filled with power drive
Put and be connected, more than one stirring paddle is installed vertically on shaft, be provided with the inwall of cell body
The equal indention of work surface of more than one fixed blade, stirring paddle and fixed blade, the top of cell body
Charging aperture and size circulations entrance are offered, the bottom of cell body offers discharging opening and size circulations outlet,
The inclined bottom surface of cell body is arranged, and the inlet of pump is connected with discharging opening pipeline, the liquid outlet of pump respectively with slurry
Material loop head and the connection of slurry collection device pipeline.
In this patent, the cooperation alr mode of stirring paddle and fixed blade is employed in hollander tub, and
Adopt circulation beating to obtain more preferable mixing effect.However, due to filter cake, sometimes viscosity is very big (i.e. high
Viscous filter cake), after being directly put in hollander tub, because the crushing effect of stirring paddle it is limited after all, so
Adding can not soon be disperseed after hollander tub, still have bulk slurry because self gravitation reason is rapid
Sink to bottom and block discharging opening, while arranging fixed blade, deflection plate etc. on the wall of hollander tub
Its broken and mixing effect can be caused because filter cake is deposited thereon to be deteriorated.Therefore, existing hollander tub is general
Poor all over there is mixing effect, mixing time length, slurry are discharged difficult and there are problems that.
The content of the invention
For drawbacks described above of the prior art or deficiency, the invention provides a kind of filter cake is into sizing device,
Filter cake can be fully crushed, mixing effect is good, into slurry efficiency high, the discharging opening for effectively alleviating beating tank is blocked up
Plug and bottom deposit.
For achieving the above object, the invention provides a kind of filter cake is into sizing device, including the interior stirring paddle that sets
Beating tank and banded extruder, the banded extruder has charging aperture and material extrusion outlet, and the port of the material extrusion outlet sets
There is screen cloth, the material extrusion outlet is stretched in the tank body of the beating tank, from the filter cake that the charging aperture is added
Filter cake extrusion can be squeezed into by the banded extruder, filter cake extrusion passes through the sieve in the material extrusion exit
Net is entered in the tank body, to form serosity under the stirring of the stirring paddle after being disperseed.
Preferably, the banded extruder has water inlet, and the water inlet is communicated to the inner chamber of the material extrusion outlet
In；
Or, water inlet is provided with the top of the beating tank, the water entered by the water inlet flows into tank body
In；
Wherein, the filter cake extrusion is disperseed after the screen cloth by the shear force of water, so as to be formed
Slurry is entered in the tank body.
Preferably, the screen cloth is the equidistant grid type screen cloth of 8～32 purposes.
Preferably, the filter cake also includes stirring motor into sizing device, and the stirring paddle includes interior stirring paddle
With outer stirring paddle, it is set in outside the interior stirring paddle, the stirring electricity the outer stirring paddle spaced radial
Machine can separately drive the interior stirring paddle and outer stirring paddle by shaft, and can be simultaneously
Drive the interior stirring paddle and outer stirring paddle rotating Vortex or reverse rotation.
Preferably, the stirring motor can drive the interior stirring paddle and outer stirring paddle vertical lifting.
Preferably, the shaft includes interior shaft and outer shaft, and the outer shaft is hollow axle,
The interior shaft passes axially through the outer shaft；
The interior stirring paddle is propeller, and the propeller blade of the propeller is from the interior shaft
Bottom extend downwardly in the shape of a spiral；
The outer stirring paddle is cage type stirring paddle, and the cage type stirring paddle is formed as ball or elliptical shape ball shape
Cage body structure, the cage body structure is connected to the bottom of the outer shaft and cage body inner chamber accommodates the spiral shell
Rotation stirring paddle, the cage body structure includes multiple corresponding circular blades or oval blade, multiple described
Circular blade or oval blade are intervally arranged to form the cage along the circumferencial direction of the cage body structure
The skeleton of body structure.
Preferably, the smallest radial spacing between the propeller and the cage type stirring paddle is
5mm～20mm.
Preferably, the inner bottom surface of the beating tank is in arc-shaped, and the radian of the inner bottom surface is less than ball or ellipse
The bottom surface radian of the cage body structure of ball shape.
Preferably, it is described beating tank inner bottom surface radian be π/3～π, the bottom surface of the cage body structure
Radian is pi/2～π.
Preferably, the beating tank also includes protection cap, and the protection cap is openably covered and covered in the tank body
Top.
Preferably, the stirring motor is arranged on outside the protection cap, and in the protection cap insertion is formed with
Hole, the periphery of the through hole is provided with earthquake washer, and the shaft passes through vertically downwardly the crash roll
Enclose to stretch in the tank body.
By above-mentioned technical proposal, directly past beating is changed in sizing device, first in the filter cake of the present invention
The mode of input filter cake in slurry tank, but the extrusion for passing through banded extruder, extrusion again by the dispersion of screen cloth,
Even meet water to enter back in beating tank into pulp-like, thus substantially alleviate the load of stirring paddle, stir
Oar need not undertake excessive crushing function, and the filter cake for being also avoided that bulk sinks to bottom and blocks discharging opening, or
Person is sticked on stirring paddle.Additionally, additionally using Double-layer stirring paddle, can reversely stir, further
Improve mixing effect, and stirring paddle liftable such that it is able to solve the deposition of beating pot bottom, realize
More fully stir, improve into slurry efficiency.
Other features and advantages of the present invention will be described in detail in subsequent specific embodiment part.
Description of the drawings
Accompanying drawing is, for providing a further understanding of the present invention, and to constitute the part of description, with
Detailed description below is used to explain the present invention together, but is not construed as limiting the invention.
In accompanying drawing：
Fig. 1 is the structural representation according to the filter cake of the preferred embodiment of the present invention into sizing device；
Fig. 2 is the top view of Fig. 1 devices, wherein eliminating protection cap to show the stirring paddle in beating tank；
Fig. 3 is the top view of Fig. 1 devices with protection cap；
Fig. 4 be Fig. 1 shown in device in be arranged on material extrusion exit screen cloth front view.
Description of reference numerals
The 1 beating banded extruder of tank 2
The stirring motor of 3 screen cloth 4
The outer shaft of shaft 6 in 5
The outer stirring paddle of stirring paddle 8 in 7
9 earthquake washers
The protection cap of 11 tank body 12
81 circular blades or the oval serum outlet of blade 13
The material extrusion of 21 charging aperture 22 is exported
23 orifice plates
Specific embodiment
The specific embodiment of the present invention is described in detail below in conjunction with accompanying drawing.It should be appreciated that
Specific embodiment described herein is merely to illustrate and explains the present invention, is not limited to this
It is bright.
In the present invention, in the case where contrary explanation is not made, the noun of locality for using as " upper and lower, top,
Bottom " be typically it is for direction shown in the drawings for or for it is vertical, vertically or on gravity direction
For each part mutual alignment relationship description word；The paper that " vertical direction " refers to illustrate is upper and lower
Direction, " horizontal " is worth the approximate horizontal paper left and right directions for being diagram；" inside and outside " is often referred to
It is radially inner and outer inside and outside the chamber for chamber or for the center of circle, center.
As shown in figure 1, the invention provides a kind of filter cake is into sizing device, the device includes interior setting stirring paddle
Beating tank 1 and banded extruder 2, the banded extruder have charging aperture 21 and material extrusion outlet 22, the material extrusion goes out
The port of mouth 22 is provided with screen cloth 3, and the tank bodies 11 of the beating tank 1 are stretched in the material extrusion outlet 22
Interior, the filter cake added from the charging aperture 21 can be squeezed into filter cake extrusion by the banded extruder 2, filter
Cake extrusion is entered in the tank body 11 after being disperseed by the screen cloth 3 at material extrusion outlet 22,
To form serosity under the stirring of the stirring paddle.Wherein screen cloth 3 is located at the top of stirring paddle, this enforcement
Screen cloth 3 and cage type stirring paddle are at a distance of 1mm-10mm in mode.
Wherein, different from prior art beating tank (groove) the mode for being directly added into filter cake, by filter cake
(especially high viscous filter cake) puts into the charging aperture 21 of banded extruder 2, extruding masterpiece of the filter cake in banded extruder 2
With lower by orifice plate 23, the circular hole aperture of orifice plate 23 is, for example, 1cm～5cm, so as to form 1cm～5cm
Round stripe shape filter cake extrusion, material extrusion outlet 22 at, circle stripe shape filter cake extrusion crushed and divided by screen cloth 3
Fritter is dissipated into, or even water can be met into slurry, so as in the work for fundamentally alleviating the stirring paddle in beating tank
Load, fritter filter cake bar can more easily be stirred oar and be sufficiently stirred for, and is difficult to result in blockage and deposits.
Specifically, it is the dispersion of promotion circle stripe shape filter cake extrusion, mitigates the pressure-bearing of screen cloth 3, banded extruder 2
There can be high pressure intake (not shown), the high pressure intake is communicated in the inner chamber of material extrusion outlet 22,
So that filter cake extrusion passes through again screen cloth 3 after mixing with water, it is easier to disperseed and formed slurry.Or,
In the case where the top of beating tank 1 is provided with water inlet (not shown), the water entered by top water inlet
Can flow directly in the tank body 11 of beating tank 1, while filter cake extrusion is disperseed and in water by screen cloth 3
Shear force under disperseed and be thoroughly mixed to form slurry.As shown in figure 4, screen cloth 3 is corrosion-resistant
Metallic sieve, the equidistant grid type screen cloth of preferably 8～32 purposes.Those skilled in the art can manage
Solution, the installation direction of screen cloth 3, shape and mesh mesh number etc. can be optimized according to concrete operating mode
Select, it is not described in detail herein.
Filter cake also includes stirring motor 4 into sizing device, and stirring paddle is preferably Double-layer stirring paddle, including interior stirs
Oar 7 and outer stirring paddle 8 are mixed, is set in outside interior stirring paddle 7 spaced radial of outer stirring paddle 8, stirring electricity
Machine 4 can separately drive interior stirring paddle 7 and outer stirring paddle 8 with different rotating speeds rotation by shaft
Turn, and can simultaneously drive interior stirring paddle 7 and the rotating Vortex of outer stirring paddle 8 or reverse rotation.So,
Using the inside and outside Double-layer stirring paddle being arranged, be conducive to being sufficiently stirred for, granule fragmentation, increase liquid fluidity,
Stirring efficiency is improved, the filter cake extrusion (or slurry) after dispersion can form high concentration after being sufficiently stirred for
Oar liquid.
Wherein, interior stirring paddle 7 and outer stirring paddle 8 also can be driven by single stirring motor 4 and be unified
Synchronous rotary, that is, share single shaft.Also can be as shown in Figure 1 respectively have different shafts,
So as to realize independent control, reverse rotation etc., to meet the stirring requirement of different levels.Referring to Fig. 1,
Shaft therein includes interior shaft 5 and outer shaft 6, and the outer shaft 6 is hollow axle, is inside stirred
Mix axle 5 and pass axially through outer shaft 6.Interior stirring paddle 7 is preferably propeller, the auger
Oar includes single propeller blade, is made up of the higher resistant material of intensity, and propeller blade is from interior stirring
The bottom of axle 5 extends downwardly in the shape of a spiral at a certain angle；Wherein, the radial dimension of helix is from centre
Portion to two ends are gradually reduced.
Outer stirring paddle 8 is preferably cage type stirring paddle, and the cage type stirring paddle is formed as ball or elliptical shape ball shape
Cage body structure, the cage body structure is connected to the bottom of outer shaft 6 and cage body inner chamber accommodates spiral and stirs
Mix oar.Cage body structure is made up of multiple corresponding circular blades or oval blade 81, multiple circular oars
Leaf or oval blade 81 are intervally arranged to form the skeleton of cage body structure along the circumferencial direction of cage body structure
(or claiming framework).For example shown in Fig. 1 and Fig. 2, outer stirring paddle 8 therein is oval cage body structure,
Including two oval blades, two oval blades are overlapped in the bottom of outer shaft 6 at top, and
And two oval blades also overlap in bottom, to form the framework of cage body.Preferably, cage type
Stirring paddle can be made up of 2-8 blade, and every blade is the impartial resistant material of thickness,
All blades are connected with top and bottom.
Due to the independent control of inside and outside stirring paddle, the two not can contact in order to avoid mechanical interference, according to general work
Skill requirement, in the present embodiment, it is desirable between the smallest radial between propeller and cage type stirring paddle
Away from for 5mm～20mm, to reach preferably stirring and flow of fluid effect.
In addition, to solve the problems, such as bottom deposit, stirring motor 4 is preferably capable driving interior stirring paddle 7
With the vertical lifting of outer stirring paddle 8.Accordingly, the inner bottom surface for being beaten tank 1 is in preferably arc-shaped, and this is interior
The radian of bottom surface is less than ball or the bottom surface radian of the cage body structure of elliptical shape ball shape.Preferably, it is beaten tank
The radian of 1 inner bottom surface is π/3～π, and the bottom surface radian of cage body structure is pi/2～π, so as in bulk
Filter cake block be deposited on beating tank 1 bottom centre when, can drive cage type stirring paddle decline be close to beating
The inner bottom surface center of tank 1, in the case of reversely rotating in inside and outside stirring paddle, by negative pressure absorbing
Mode, deposit is sucked and is stirred in cage body, increases mixed flow, can so as to pass through lifting stirring slurry
Effectively solving sediment, it is to avoid filter cake sediment blocks serum outlet 13.
Referring to Fig. 1, beating tank 1 also includes protection cap 12, and the protection cap 12 is openably covered and covered in tank
The top of body 11, on the one hand can prevent because the too fast caused slurry of rotating speed of agitator splashes, another
Aspect can prevent the dust of outside or other pollutions from entering in beating tank 1.Protection cap 12 is being installed
When, stirring motor 4 can be arranged on outside protection cap 12, the hole than shaft is formed with protection cap 12
The slightly larger through hole in footpath, as shown in figure 3, the periphery of the through hole is provided with earthquake washer 9, shaft is erected
It is straight down to pass through earthquake washer 9 to stretch in tank body.Earthquake washer 9 is prevented to protect stirring paddle
Stirring paddle and the directly contact of protection cap 12, cause to wear and tear or damage.Slurry is provided with the bottom of beating tank 1
Liquid outlet 13, when concentration of slurry reaches setting value (such as 5%～50%), starts discharging.Work as serosity
Concentration is reached setting value and starts after discharging, to be started to supplement fresh water by water inlet.
Embodiment
Using the filter cake shown in Fig. 1 into sizing device.Wherein, the filter cake treating capacity of banded extruder 2 is
0.1-10kg/h, the aperture of the orifice plate 23 of banded extruder is 1-5cm, and propeller rotating speed is controlled to 0～600
R/min, cage type rotating speed of agitator is 0～900r/min, and the two reverse rotation, screen cloth 3 is 8～32 purposes
Equidistant grid type screen cloth, earthquake washer 9 is the specification of diameter 2-5cm, to obtaining concentration of slurry
0%～50% final serosity.
Filter cake includes step into the operational approach of slurry：
1st, the charging aperture 21 that filter cake passes through banded extruder 2, into banded extruder 2；
2nd, filter cake is extruded under the pressure effect of banded extruder 2 by the orifice plate 23 of the front end of banded extruder 2
Into circle stripe shape filter cake extrusion；
3rd, filter cake extrusion eventually arrives at the screen cloth 3 arranged at the material extrusion outlet 22 of banded extruder 2；
4th, filter cake extrusion is disperseed in screen cloth 3 by the active force of water；
5th, propeller is controlled by stirring motor 4 and cage type stirring paddle is coaxially rotated backward；
6th, while lifting stirring paddle, control stirring paddle was moved to vertically downward from beating at interval of 5 minutes
The bottom 5mm of slurry tank 1, is kept for 1 minute, is then resetted；
7th, when concentration of slurry reaches setting value, slurry starts to be discharged from serum outlet 13；
8th, start to discharge after slurry, open back with water inlet line and supplement fresh water.
Table one：Each control parameter, beating time and beating resultses
In the above-described embodiments, it is visible referring to table one, using the filter cake of apparatus of the present invention into slurry efficiency high,
Controllable into slurry speed, filter cake deposition is low, can be prevented effectively from serum outlet blocking and be beaten pot bottom
Sediment.Moreover it is possible to effectively reduce stirring paddle load, energy-saving effect is played, and prevented because stirring paddle turns
The splashing that fast height is caused, and outside dust fall etc..
The preferred embodiment of the present invention is described in detail above in association with accompanying drawing, but, the present invention is not limited
Detail in above-mentioned embodiment, in the range of the technology design of the present invention, can be to the present invention
Technical scheme carry out various simple variants, such as the concrete shape of inside and outside stirring paddle also internal can be adopted
Cage type stirring paddle, and outside propeller using major diameter etc., these simple variants are without departing from this
The design of invention, thus belong to protection scope of the present invention.
It is further to note that each particular technique described in above-mentioned specific embodiment is special
Levy, in the case of reconcilable, can be combined by any suitable means, in order to avoid need not
The repetition wanted, the present invention is no longer separately illustrated to various possible compound modes.
Additionally, combination in any can also be carried out between a variety of embodiments of the present invention, as long as its
Without prejudice to the thought of the present invention, it should equally be considered as content disclosed in this invention.
Claims (11)
1. a kind of filter cake is into sizing device, including the interior beating tank (1) for setting stirring paddle, it is characterised in that
The filter cake also includes banded extruder (2) into sizing device, and there is the banded extruder charging aperture (21) and material extrusion to go out
Mouth (22), the port of material extrusion outlet (22) is provided with screen cloth (3), and the material extrusion exports (22)
Stretch in the tank body (11) of beating tank (1), from the filter cake energy that the charging aperture (21) is added
Enough to be squeezed into filter cake extrusion by the banded extruder (2), the filter cake extrusion is exported (22) in the material extrusion
Place is entered in the tank body (11), with the stirring paddle after being disperseed by the screen cloth (3)
Serosity is formed under stirring.
2. filter cake according to claim 1 is into sizing device, it is characterised in that：
With water inlet, the water inlet is communicated to material extrusion outlet (22) to the banded extruder (2)
In inner chamber；
Or, water inlet is provided with the top of beating tank (1), the current entered by the water inlet
In entering the tank body (11), the filter cake extrusion by after the screen cloth (3) by the shear action of water
Power is disperseed, interior into the tank body (11) so as to form slurry.
3. filter cake according to claim 1 is into sizing device, it is characterised in that the screen cloth (3)
For the equidistant grid type screen cloth of 8～32 purposes.
4. the filter cake according to any one in claims 1 to 3 is into sizing device, it is characterised in that
The filter cake into sizing device also include stirring motor (4), the stirring paddle include interior stirring paddle (7) and
Outer stirring paddle (8), is set in the interior stirring paddle (7) outward outer stirring paddle (8) spaced radial,
The stirring motor (4) can separately drive the interior stirring paddle (7) and outer by shaft
Stirring paddle (8), and can simultaneously drive the interior stirring paddle (7) and outer stirring paddle (8) to revolve in the same direction
Turn or reversely rotate.
5. filter cake according to claim 4 is into sizing device, it is characterised in that the stirring motor
(4) the interior stirring paddle (7) and outer stirring paddle (8) vertical lifting can be driven.
6. filter cake according to claim 5 is into sizing device, it is characterised in that the shaft bag
Interior shaft (5) and outer shaft (6) are included, the outer shaft (6) is hollow axle, the interior stirring
Axle (5) passes axially through the outer shaft (6)；
Wherein, the interior stirring paddle (7) is propeller, the propeller blade of the propeller from
The bottom of the interior shaft (5) extends downwardly in the shape of a spiral；
The outer stirring paddle (8) is cage type stirring paddle, and the cage type stirring paddle is formed as ball or elliptical shape ball
The cage body structure of shape, the cage body structure is connected to the bottom of the outer shaft (6) and cage body inner chamber
The propeller is accommodated, the cage body structure includes multiple corresponding circular blades or oval oar
Leaf (81), multiple circular blades or oval blade (81) are along the circumference side of the cage body structure
To being intervally arranged to form the skeleton of the cage body structure.
7. filter cake according to claim 6 is into sizing device, it is characterised in that the auger
Smallest radial spacing between oar and the cage type stirring paddle is 5mm～20mm.
8. filter cake according to claim 6 is into sizing device, it is characterised in that the beating tank (1)
Inner bottom surface be in arc-shaped, the radian of the inner bottom surface is less than ball or the cage body structure of elliptical shape ball shape
Bottom surface radian.
9. filter cake according to claim 8 is into sizing device, it is characterised in that the beating tank (1)
The radian of inner bottom surface be π/3～π, the bottom surface radian of the cage body structure is pi/2～π.
10. filter cake according to claim 4 is into sizing device, it is characterised in that the beating tank (1)
Also include protection cap (12), the protection cap (12) is openably covered and covered on the top of the tank body (11)
Portion.
11. filter cakes according to claim 10 are into sizing device, it is characterised in that the stirring electricity
Machine (4) is arranged on the protection cap (12) outward, and on the protection cap (12) through hole is formed with,
The periphery of the through hole is provided with earthquake washer (9), and the shaft passes through vertically downwardly the crash roll
Enclose (9) to stretch in the tank body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510696472.XA CN106606949B (en) | 2015-10-23 | 2015-10-23 | Filter cake is at sizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510696472.XA CN106606949B (en) | 2015-10-23 | 2015-10-23 | Filter cake is at sizing device |
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| Publication Number | Publication Date |
|---|---|
| CN106606949A true CN106606949A (en) | 2017-05-03 |
| CN106606949B CN106606949B (en) | 2019-04-02 |
Family
ID=58612920
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510696472.XA Active CN106606949B (en) | 2015-10-23 | 2015-10-23 | Filter cake is at sizing device |
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| CN (1) | CN106606949B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107500505A (en) * | 2017-09-20 | 2017-12-22 | 华北理工大学 | A kind of high efficiency river sludge collection and treatment device |
| CN107620213A (en) * | 2017-08-31 | 2018-01-23 | 海宁文硕科技咨询有限公司 | A kind of anti-crease finishing method for fabric |
| CN107653680A (en) * | 2017-08-31 | 2018-02-02 | 海宁文硕科技咨询有限公司 | A kind of antibacterial finishing process for fabric |
| CN107675492A (en) * | 2017-08-31 | 2018-02-09 | 海宁文硕科技咨询有限公司 | A kind of preparation method of luminescent warm-keeping fabric |
| CN107700225A (en) * | 2017-08-31 | 2018-02-16 | 海宁文硕科技咨询有限公司 | A kind of processing method of blended yarn weaved fabric |
| CN109550451A (en) * | 2018-09-30 | 2019-04-02 | 中国水利水电科学研究院 | A kind of energy-efficient desulfurization pulping device |
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| CN202983562U (en) * | 2012-12-03 | 2013-06-12 | 龙星化工股份有限公司 | Stirring liquefying device of white carbon black filter cakes |
| CN204220057U (en) * | 2014-10-16 | 2015-03-25 | 河北京鹏环保科技有限公司 | The pulping device of a kind of automatic water supplement and lime |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202983562U (en) * | 2012-12-03 | 2013-06-12 | 龙星化工股份有限公司 | Stirring liquefying device of white carbon black filter cakes |
| CN204220057U (en) * | 2014-10-16 | 2015-03-25 | 河北京鹏环保科技有限公司 | The pulping device of a kind of automatic water supplement and lime |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107620213A (en) * | 2017-08-31 | 2018-01-23 | 海宁文硕科技咨询有限公司 | A kind of anti-crease finishing method for fabric |
| CN107653680A (en) * | 2017-08-31 | 2018-02-02 | 海宁文硕科技咨询有限公司 | A kind of antibacterial finishing process for fabric |
| CN107675492A (en) * | 2017-08-31 | 2018-02-09 | 海宁文硕科技咨询有限公司 | A kind of preparation method of luminescent warm-keeping fabric |
| CN107700225A (en) * | 2017-08-31 | 2018-02-16 | 海宁文硕科技咨询有限公司 | A kind of processing method of blended yarn weaved fabric |
| CN108654495A (en) * | 2017-08-31 | 2018-10-16 | 海宁文硕科技咨询有限公司 | A kind of device for formulating |
| CN108729239A (en) * | 2017-08-31 | 2018-11-02 | 海宁文硕科技咨询有限公司 | The processing method of modified blended yarn weaved fabric |
| CN107500505A (en) * | 2017-09-20 | 2017-12-22 | 华北理工大学 | A kind of high efficiency river sludge collection and treatment device |
| CN109550451A (en) * | 2018-09-30 | 2019-04-02 | 中国水利水电科学研究院 | A kind of energy-efficient desulfurization pulping device |
| CN109550451B (en) * | 2018-09-30 | 2021-03-12 | 中国水利水电科学研究院 | Energy-conserving efficient pulping device for desulfurization |
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|---|---|
| CN106606949B (en) | 2019-04-02 |
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