CN204715117U - The speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid is separated - Google Patents
The speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid is separated Download PDFInfo
- Publication number
- CN204715117U CN204715117U CN201520329288.7U CN201520329288U CN204715117U CN 204715117 U CN204715117 U CN 204715117U CN 201520329288 U CN201520329288 U CN 201520329288U CN 204715117 U CN204715117 U CN 204715117U
- Authority
- CN
- China
- Prior art keywords
- cone cylinder
- aniseed
- liquid slurry
- small powder
- particle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
Links
Abstract
The utility model provides the speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid is separated, and mainly comprises inlet duct, air-flow vortex breaker and liquid slurry generating apparatus.Be characterized in that the combined type feed liquid of extra quality cone cylinder is separated, first adopt speed change air-flow vortex kinetic energy particle, rear mixing with aqueous water generates slurries.The utility model is large oval by crucial cross section, little ellipse, great circle and roundlet realize becoming and accelerate eddy flow fragmentation, prevent " revolving cake " phenomenon, improve crushing efficiency, particle is transition at the uniform velocity, filtrate raises speed, rapid mixing without blocking conveying and particle stirs, by the fairing of inlet duct, round-corner transition reduces air motion resistance, reduction energy consumption and difference in diameter design realize air-flow pressurization speed-raising, realize particle screening by particle filter and prevent particle from blocking, realize adding water by the grid-shaped water inlet containing slot, be vented and prevent from falling into larger foreign matter.
Description
Technical field
The utility model relates to the speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid is separated, particularly relating to a kind of is large ellipse by crucial cross section, little ellipse, great circle and roundlet realize becoming and accelerate eddy flow fragmentation, prevent " revolving cake " phenomenon, improve crushing efficiency, particle is transition at the uniform velocity, filtrate raises speed, rapid mixing without blocking conveying and particle stirs, by boring cylinder with aniseed, the aniseed cone cylinder admission line that small powder cone cylinder upper end outer ledge is tangent, small powder cone cylinder admission line generates low energy loss circulation, by the fairing of inlet duct, round-corner transition reduces air motion resistance, reduction energy consumption and difference in diameter design realize air-flow pressurization speed-raising, realize particle screening by particle filter and prevent particle from blocking, realize adding water by the grid-shaped water inlet containing slot, be vented and prevent from falling into larger foreign matter, belong to the technical research field of paper-making industry pulping equipment.
Background technology
In paper industry, the generation of paper pulp needs pulpboard, waste and old books, waste carton etc. to put into hydrabrusher, and carries out size degradation by the rotation of rotor, to make unit for uniform suspension.But due to the unicity of current pulper working method and structure, cause following problem: one is that efficiency is low, existing pulper mainly accelerates the decomposition of particle by the mixed liquor stirring particle and water, the decomposition rate of particle often depends on the mixing speed of rotor, and in pulping process, some energy ezpenditure, on the reactive loss of machinery, therefore causes the efficiency of machinery pulping very low; Two is that energy consumption is large, and pulper is operationally because relying on the stirring of aqueous water to decompose, and make pulp kneader rotor in motion process, not only want carry fluid to rotate, but also will overcome the resistance of fluid, this consumes a large amount of mechanical energy to a certain extent; Three is that easy formation " revolves cake ", existing pulper especially drum-shaped structure, when be at the uniform velocity stir time, because the relative velocity of particle and water is inactive state, easily form " revolving cake ", thus make pulper lose pulping function.
Therefore,, energy consumption low for efficiency ubiquitous in existing pulping equipment is large and easily form problems such as " revolving cake ", should consider from pulper working method and structure, design that pulping efficiency is high, energy consumption is low and without a kind of pulping equipment of " revolving cake ".
Summary of the invention
The efficiency that the utility model exists for existing pulping equipment is low, energy consumption large and the problems such as easy formation " revolving cake ", provides the speed change air-flow vortex kinetic energy pulping equipment that a kind of a kind of combined type feed liquid that can effectively solve the problem is separated.
The speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid of the present utility model is separated is by the following technical solutions:
The speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid is separated, mainly comprise inlet duct, air-flow vortex breaker and liquid slurry generating apparatus, described inlet duct is primarily of air inlet conveying supervisor, aniseed cone cylinder admission line, air inlet conveying arm and small powder cone cylinder admission line composition, the end of air inlet conveying supervisor is connected with aniseed cone cylinder admission line and air inlet conveying arm, aniseed cone cylinder admission line and small powder cone cylinder admission line are arranged on the outer ledge place, upper end of aniseed cone cylinder and small powder cone cylinder respectively, the end of air inlet conveying arm is connected with small powder cone cylinder admission line, described air-flow vortex breaker is primarily of aniseed cone cylinder and small powder cone cylinder composition, aniseed cone cylinder and small powder cone cylinder are surrounded by material cone barrel respectively, and material cone cover is installed in respective upper end, particle filter is separately installed with in aniseed cone cylinder and small powder cone cylinder, particle filter is provided with some filtration internal taper holes, material cone cylinder clamp is installed outside material cone barrel, the crucial cross section of aniseed cone cylinder and small powder cone cylinder working region is from top to bottom large oval cross section, little oval cross section, large circular section and little circular section, region between large oval cross section and little oval cross section is particle fracture area, region between little oval cross section and large circular section is particle filter buffer, region between large circular section and little circular section is filtrate accelerating region, region below little circular section is filtrate delivery area, described liquid slurry generating apparatus liquid slurry case and liquid slurry case lid composition, liquid slurry case is built with the mixed liquor of aqueous water and filtrate, liquid slurry case bottom surface is provided with pillar, liquid slurry case lower end side is provided with discharging opening, liquid slurry case lid has two circular holes, for installing aniseed cone cylinder and small powder cone cylinder, liquid slurry case lid there are 2 groups of liquid slurry case lid draw-in grooves, be distributed in the periphery of two circular holes, liquid slurry case lid draw-in groove is used for batch cone cylinder clamp, and fixing aniseed cone cylinder and small powder cone cylinder, in addition, liquid slurry case lid has 3 groups of equidistant water inlets side by side.
Described aniseed cone cylinder and small powder cone cylinder are the elliptical table shape structure of upper big, lower small, and the major axis of its large oval cross section is
a 1, minor axis is
b 1, the major axis of little oval cross section is
a 2, minor axis is
b 2and
a 2=2
a 1/ 3,
b 2=2
b 1/ 3, the diameter of large circular section is
d 1and
d 1=
b 2, the diameter of little circular section is
d 2and
d 2=
d 1/ 3, the height of particle fracture area is
h 1, the height of particle filter buffer is
h 2and
h 2=
h 1/ 5, the height of filtrate accelerating region is
h 3and
h 3=
h 1/ 3, the height of filtrate delivery area is
h 4and
h 4=
h 1; Described material cone cylinder clamp is 4, is circumferentially uniformly distributed.
It is tangent that cylinder admission line bored by described aniseed, small powder cone cylinder admission line bores cylinder with aniseed respectively, small powder bores cylinder upper end outer ledge, and material cone cover is ellipsoidal structure; Described air inlet conveying supervisor is fairing transition to air inlet conveying arm, and the diameter of air inlet conveying supervisor is
d 3and
d 3=
d 1/ 2, the diameter of air inlet conveying arm is
d 4and d
4=
d 1/ 4, there is fillet air inlet conveying supervisor and aniseed cone cylinder admission line junction
r 1transition, there is fillet air inlet conveying arm and small powder cone cylinder admission line junction
r 2transition and
r 2=
r 1/ 2.
Described particle filter is the disc-shaped structure containing some filtration internal taper holes; Described filtration internal taper hole is the truncated cone-shaped structure of upper big, lower small, and upper bore dia is
Φ d 5and
Φ d 5=
Φ d 1/ 8, lower bore dia is
Φ d 6and
Φ d 6=
Φ d 1/ 24.
Shown in liquid slurry case be cuboid groove structure, liquid slurry case lid is rectangle structure, and the water inlet on liquid slurry case lid is grid-shaped structure, and is made up of 8 slots, and the liquid slurry case lid draw-in groove on liquid slurry case lid often group is 4 and even circumferential circle distribution; Described pillar is 6, is distributed in cuboid groove bottom corner and middle part.
The utility model aniseed is bored cylinder and small powder cone cylinder is designed to greatly upper, lower little elliptical table shape structure, and its crucial cross section is large oval cross section, little oval cross section, large circular section and little circular section, realize gas by this design and produce change acceleration eddy flow in material cone cylinder, thus increase air-flow vortex to the crushing force of particle and realize with the variable motion in cross section, namely after compressed air enters material cone cylinder, both can reduce gradually along with cross-sectional area, eddy flow is impelled constantly to accelerate, the kinetic energy of air-flow vortex increases gradually, thus make vortex drive particle mutually to collide, larger momentum is had time broken, the acceleration of air-flow can be realized again in elliptical trajectory, retarded motion, prevent air-flow because at the uniform velocity producing " revolving cake " phenomenon, and improve particle efficiency by the gear shift shock of air-flow, be large oval cross section, little oval cross section by the upper and lower Cross section Design of particle fracture area, the change being produced particle by this design is accelerated broken, and by larger height h
1increase the collision frequency of particle, be little oval cross section, large circular section by the upper and lower Cross section Design of particle filter buffer, air-flow and particle is realized by speed change to transition at the uniform velocity by this design, and make particle even by particle filter under state at the uniform velocity, prevent the pulping of speed change from only passing through in a certain region of particle filter, be large circular section, little circular section by the upper and lower Cross section Design of filtrate accelerating region, realized the acceleration of filtrate by this design, thus enter liquid slurry case with larger momentum, and play the effect of stirring liquid slurry, thus generate even liquid slurry, filtrate delivery area is designed to prismatic circle, keeps the speed of filtrate and air-flow with this, and the conveying capacity of filtrate, and prevent filtrate from blocking in course of conveying.
Aniseed is bored cylinder admission line by the utility model, small powder cone cylinder admission line bores cylinder with aniseed respectively, small powder cone cylinder upper end outer ledge is tangent, tangential inlet circulation can be formed by this design, reduce airflow kinetic energy loss, namely pressure-air is input to aniseed cone cylinder admission line, during small powder cone cylinder admission line, because of aniseed cone cylinder admission line, small powder cone cylinder admission line bores cylinder with aniseed respectively, tangent and the non-structure sudden change of small powder cone cylinder upper end outer ledge, pressure-air can be made to enter aniseed cone cylinder, during small powder cone cylinder, still can keep motion at a high speed, and bore cylinder with the state of minimum kinetic energy loss at aniseed, tangential rotary motion is done in small powder cone cylinder, air inlet conveying supervisor fairing is transitioned into air inlet conveying arm, air inlet conveying supervisor and aniseed are bored cylinder admission line junction and air inlet conveying arm and small powder cone cylinder admission line junction and are adopted round-corner transition, can be reduced air motion resistance by this structural design, be reduced energy consumption, the diameter design of arm air inlet is carried to be the half that air inlet conveying is responsible for, air-flow can be made in air inlet conveying arm and small powder cone cylinder admission line still to keep larger kinetic energy by this design, namely to pressurize speed-raising by reducing the sectional area of fluid motion, ensureing that boring air-flow vortex kinetic energy particle in cylinder for small powder provides required high-speed gas.
Particle filtering device designs is the disc-shaped structure filtering internal taper hole containing some upper big, lower small by the utility model, by this design, there is following effect: one is screening particle, only have more short grained particle can enter particle filter buffer, ensure the even particle size of liquid slurry, two is prevent blocking, if larger particle particle enters into filtration internal taper hole, when eddy flow is filtering internal taper hole upper surface through will forming certain back pressure later, back pressure will produce suction, and the truncated cone-shaped structure of upper big, lower small will make the sucking-off easily of particle particle.
The utility model the design of intake starched by liquid on case lid is the grid-shaped structure containing 8 slots, and can be realized the discharge of gas in the interpolation of aqueous water, liquid slurry case by this design, can prevent again larger foreign matter from entering liquid slurry case, contaminated liquid is starched; Liquid slurry case lid has 4 equally distributed liquid slurry case lid draw-in grooves, material can be made to bore cylinder clamp by this design and snap in groove, play the effect of fixing aniseed cone cylinder, small powder cone cylinder; Design 6 pillars altogether in cuboid groove bottom corner and middle part, can be by this design the stability that whole pulping equipment provides support and maintenance equipment runs, what produce during abatement apparatus runs rocks.
The beneficial effects of the utility model are: bore that crucial cross section in cylinder, small powder cone cylinder is large oval cross section by aniseed, little oval cross section, large circular section and little circular section design produce become accelerate eddy flow broken, prevent " rotations " phenomenon, improve crushing efficiency, and formed become accelerate broken particle fracture area, at the uniform velocity transition particle filter buffer, filtrate speed-raising filtrate accelerating region, stir without the filtrate delivery area of blocking and the rapid mixing of particle and generate even liquid and starch; By boring cylinder with aniseed, small powder bores that cylinder admission line bored by outer ledge tangent aniseed in cylinder upper end, small powder bores the gas circulating that cylinder admission line realizes minimum energy loss; Air inlet conveying is responsible for, the fairing transition of air inlet conveying arm, and air inlet conveying supervisor and aniseed cone cylinder admission line junction, air inlet carry the round-corner transition of arm and small powder cone cylinder admission line junction to reduce air motion resistance, reduce energy consumption; The half design being air inlet conveying supervisor by the diameter of air inlet conveying arm realizes pressurization speed-raising; By realizing screening particle containing the particle filter filtering internal taper hole and prevent particle from blocking; Realize adding aqueous water, being vented and preventing to enter larger foreign matter by the grid-shaped water inlet containing slot; By material cone cylinder clamp and liquid slurry case lid draw-in groove realization fixing aniseed cone cylinder, the small powder cone cylinder of 4 circumference uniform distributions.
Accompanying drawing explanation
Fig. 1 is the integrally-built schematic front view of the utility model.
Fig. 2 is the integrally-built schematic top plan view of the utility model.
Fig. 3 is the schematic three dimensional views of the utility model air-flow vortex breaker.
Fig. 4 is the physical dimension schematic diagram of the utility model air-flow vortex breaker.
The physical dimension schematic diagram of Tu5Shi the utility model partial admission device.
Fig. 6 is the distribution schematic diagram filtering internal taper hole in the utility model particle filter.
Fig. 7 is the connection diagram of the utility model local particle filter and material cone cylinder clamp.
Wherein: 1, pillar, 2, liquid slurry case, 3, aqueous water, 4, liquid slurry case lid draw-in groove, 5, liquid slurry case lid, 6, water inlet, 7, particle filter, 8, material cone barrel, 9, material cone cover, 10, material cone cylinder clamp, 11, discharging opening, 12, aniseed cone cylinder, 13, small powder cone cylinder, 14, small powder cone cylinder admission line, 15, air inlet conveying arm, 16, aniseed cone cylinder admission line, 17, air inlet conveying supervisor, 18, little circular section, 19, large circular section, 20, little oval cross section, 21, large oval cross section, 22, particle fracture area, 23, particle filter buffer, 24, filtrate accelerating region, 25, filtrate delivery area, 26, filter internal taper hole.
Detailed description of the invention
Embodiment:
As shown in Figure 1 and Figure 2, the speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid of the present utility model is separated, mainly comprises inlet duct, air-flow vortex breaker and liquid slurry generating apparatus.Inlet duct forms primarily of air inlet conveying supervisor 17, aniseed cone cylinder admission line 16, air inlet conveying arm 15 and small powder cone cylinder admission line 14, the end of air inlet conveying supervisor 17 is connected with aniseed cone cylinder admission line 16 and air inlet conveying arm 15, aniseed cone cylinder admission line 16 and small powder cone cylinder admission line 14 are arranged on the outer ledge place, upper end of aniseed cone cylinder 12 and small powder cone cylinder 13 respectively, and the end of air inlet conveying arm 15 is connected with small powder cone cylinder admission line 14.Aniseed cone cylinder admission line 16, small powder cone cylinder admission line 14 bores cylinder 12 with aniseed respectively, small powder cone cylinder 13 upper end outer ledge is tangent, this design can form tangential inlet circulation, reduce airflow kinetic energy loss, when namely working, when pressure-air is input to aniseed cone cylinder admission line 16, small powder cone cylinder admission line 14, because of aniseed cone cylinder admission line 16, small powder cone cylinder admission line 14 bores cylinder 12 with aniseed respectively, tangent and the non-structure sudden change of small powder cone cylinder 13 upper end outer ledge, pressure-air can be made to enter aniseed cone cylinder 12, during small powder cone cylinder 13, still can keep motion at a high speed, and with the state of minimum kinetic energy loss at aniseed cone cylinder 12, tangential rotary motion is done in small powder cone cylinder 13,
Air-flow vortex breaker forms primarily of aniseed cone cylinder 12 and small powder cone cylinder 13, aniseed cone cylinder 12 and small powder cone cylinder 13 are surrounded by material cone barrel 8 respectively, and material cone cover 9 is installed in respective upper end, material cone cover 9 is ellipsoidal structure, be separately installed with particle filter 7 in aniseed cone cylinder 12 and small powder cone cylinder 13, particle filter 7 is provided with some filtration internal taper holes 26, is provided with material cone cylinder clamp 10 outside material cone barrel 8, material cone cylinder clamp 10 is 4, is circumferentially uniformly distributed.
Liquid slurry generating apparatus liquid slurry case 2 and liquid slurry case lid 5 form.Liquid slurry case 2 be cuboid groove structure, and liquid starches the mixed liquor of case 2 built with aqueous water 3 and filtrate.Liquid slurry case lid 5 is rectangle structure, liquid slurry case lid 5 has 3 groups of equidistant water inlets 6 side by side, water inlet 6 is grid-shaped structure, and be made up of 8 slots, this design can realize the discharge of gas in the interpolation of aqueous water 3, liquid slurry case 2, can prevent again larger foreign matter from entering liquid slurry case 2, contaminated liquid is starched; Liquid slurry case lid 5 also has two circular holes, for installing aniseed cone cylinder 12 and small powder cone cylinder 13, liquid slurry case lid 5 has 2 groups of liquid slurry case lid draw-in grooves 4, it is distributed in the periphery of even two circular holes, liquid slurry case lid draw-in groove 4 is for batch cone cylinder clamp 10, and fixing aniseed cone cylinder 12 and small powder cone cylinder 13.Liquid slurry case 2 bottom surface is provided with pillar 1, and pillar 1 is 6, is distributed in cuboid groove bottom corner and middle part, and this design can be the stability that whole pulping equipment provides support and maintenance equipment runs, and what produce during abatement apparatus runs rocks.Liquid slurry case 2 lower end side is provided with discharging opening 11.
As shown in Figure 3, Figure 4, aniseed cone cylinder 12 and small powder cone cylinder 13 are the elliptical table shape structure of upper big, lower small, the crucial cross section of aniseed cone cylinder 12 and small powder cone cylinder 13 working region is from top to bottom large oval cross section 21, little oval cross section 20, large little circular section, circular section 19 and 18, and the major axis of large oval cross section 21 is
a 1, minor axis is
b 1, the major axis of little oval cross section 20 is
a 2, minor axis is
b 2and
a 2=2
a 1/ 3,
b 2=2
b 1/ 3, the diameter of large circular section 19 is
d 1and
d 1=
b 2, the diameter of little circular section 18 is
d 2and
d 2=
d 1/ 3.Operationally, this design realizes gas and produce change acceleration eddy flow in material cone cylinder, thus increase air-flow vortex to the crushing force of particle and realize with the variable motion of the gas in cross section, namely after compressed air enters material cone cylinder, both can reduce gradually along with cross-sectional area, eddy flow is impelled constantly to accelerate, the kinetic energy of air-flow vortex increases gradually, thus make vortex drive particle mutually to collide, larger momentum is had time broken, the acceleration of air-flow can be realized again in elliptical trajectory, retarded motion, prevent air-flow because at the uniform velocity producing " revolving cake " phenomenon, and improve particle efficiency by the gear shift shock of air-flow.
Region between large oval cross section 21 and little oval cross section 20 is particle fracture area 22, and the height of particle fracture area 22 is
h 1, the change that this district realizes particle is accelerated broken, and by larger height h
1increase the collision frequency of particle; Region between little oval cross section 20 and large circular section 19 is particle filter buffer 23, and the height of particle filter buffer 23 is
h 2and
h 2=
h 1/ 5, this district realizes air-flow and particle by speed change to transition at the uniform velocity, and makes particle under state at the uniform velocity evenly by particle filter 7, prevents the pulping of speed change from only passing through in a certain region of particle filter 7; Region between large circular section 19 and little circular section 18 is filtrate accelerating region 24, and the height of filtrate accelerating region 24 is
h 3and
h 3=
h 1/ 3, this district realizes the acceleration of filtrate, thus enters liquid slurry case 2 with larger momentum, and plays the effect of stirring liquid slurry, thus generates even liquid slurry; Little circular section 18 take lower area as filtrate delivery area 25, and the height of filtrate delivery area 25 is
h 4and
h 4=
h 1, this district realizes the speed keeping filtrate and air-flow, and the conveying capacity of filtrate, and prevents filtrate from blocking in course of conveying.
As shown in Figure 5, air inlet conveying supervisor 17 is fairing transition to air inlet conveying arm 15, and there is fillet air inlet conveying supervisor 17 and aniseed cone cylinder admission line 16 junction
r 1transition, there is fillet air inlet conveying arm 15 and small powder cone cylinder admission line 14 junction
r 2transition and
r 2=
r 1/ 2, this structural design can reduce air motion resistance, reduce energy consumption; The diameter of air inlet conveying supervisor 17 is
d 3and
d 3=
d 1/ 2, the diameter of air inlet conveying arm 15 is
d 4and d
4=
d 1/ 4, the diameter design of arm 15 air inlet is carried to be the half that supervisor 17 is carried in air inlet, air-flow can be made in air inlet conveying arm 15 and small powder cone cylinder admission line 14 still to keep larger kinetic energy by this design, namely to pressurize speed-raising by reducing the sectional area of fluid motion, ensureing that boring air-flow vortex kinetic energy particle in cylinder 13 for small powder provides required high-speed gas.
As shown in Figure 6, Figure 7, particle filter 7 is the disc-shaped structure containing some filtration internal taper holes 16, filter the truncated cone-shaped structure that internal taper hole 26 is upper big, lower small, upper bore dia is
Φ d 5and
Φ d 5=
Φ d 1/ 8, lower bore dia is
Φ d 6and
Φ d 6=
Φ d 1/ 24, operationally, this design has following effect: one is screening particle, only has more short grained particle can enter particle filter buffer 22, ensures the even particle size of liquid slurry; Two is prevent blocking, if larger particle particle enters into filter internal taper hole 26, when eddy flow is filtering internal taper hole 26 upper surface through will forming certain back pressure later, back pressure will produce suction, and the truncated cone-shaped structure of upper big, lower small will make the sucking-off easily of particle particle.
Claims (5)
1. the speed change air-flow vortex kinetic energy pulping equipment of a combined type feed liquid separation, mainly comprise inlet duct, air-flow vortex breaker and liquid slurry generating apparatus, it is characterized in that: described inlet duct is primarily of air inlet conveying supervisor, aniseed cone cylinder admission line, air inlet conveying arm and small powder cone cylinder admission line composition, the end of air inlet conveying supervisor is connected with aniseed cone cylinder admission line and air inlet conveying arm, aniseed cone cylinder admission line and small powder cone cylinder admission line are arranged on the outer ledge place, upper end of aniseed cone cylinder and small powder cone cylinder respectively, the end of air inlet conveying arm is connected with small powder cone cylinder admission line, described air-flow vortex breaker is primarily of aniseed cone cylinder and small powder cone cylinder composition, aniseed cone cylinder and small powder cone cylinder are surrounded by material cone barrel respectively, and material cone cover is installed in respective upper end, particle filter is separately installed with in aniseed cone cylinder and small powder cone cylinder, particle filter is provided with some filtration internal taper holes, material cone cylinder clamp is installed outside material cone barrel, the crucial cross section of aniseed cone cylinder and small powder cone cylinder working region is from top to bottom large oval cross section, little oval cross section, large circular section and little circular section, region between large oval cross section and little oval cross section is particle fracture area, region between little oval cross section and large circular section is particle filter buffer, region between large circular section and little circular section is filtrate accelerating region, region below little circular section is filtrate delivery area, described liquid slurry generating apparatus liquid slurry case and liquid slurry case lid composition, liquid slurry case is built with the mixed liquor of aqueous water and filtrate, liquid slurry case bottom surface is provided with pillar, liquid slurry case lower end side is provided with discharging opening, liquid slurry case lid has two circular holes, for installing aniseed cone cylinder and small powder cone cylinder, liquid slurry case lid there are 2 groups of liquid slurry case lid draw-in grooves, be distributed in the periphery of two circular holes, liquid slurry case lid draw-in groove is used for batch cone cylinder clamp, and fixing aniseed cone cylinder and small powder cone cylinder, in addition, liquid slurry case lid has 3 groups of equidistant water inlets side by side.
2. the speed change air-flow vortex kinetic energy pulping equipment of a kind of combined type feed liquid separation as claimed in claim 1, is characterized in that: described aniseed cone cylinder and small powder cone cylinder are the elliptical table shape structure of upper big, lower small, and the major axis of its large oval cross section is
a 1, minor axis is
b 1, the major axis of little oval cross section is
a 2, minor axis is
b 2and
a 2=2
a 1/ 3,
b 2=2
b 1/ 3, the diameter of large circular section is
d 1and
d 1=
b 2, the diameter of little circular section is
d 2and
d 2=
d 1/ 3, the height of particle fracture area is
h 1, the height of particle filter buffer is
h 2and
h 2=
h 1/ 5, the height of filtrate accelerating region is
h 3and
h 3=
h 1/ 3, the height of filtrate delivery area is
h 4and
h 4=
h 1; Described material cone cylinder clamp is 4, is circumferentially uniformly distributed.
3. the speed change air-flow vortex kinetic energy pulping equipment of a kind of combined type feed liquid separation as claimed in claim 1, it is characterized in that: it is tangent that cylinder admission line bored by described aniseed, small powder cone cylinder admission line bores cylinder with aniseed respectively, small powder bores cylinder upper end outer ledge, and material cone cover is ellipsoidal structure; Described air inlet conveying supervisor is fairing transition to air inlet conveying arm, and the diameter of air inlet conveying supervisor is
d 3and
d 3=
d 1/ 2, the diameter of air inlet conveying arm is
d 4and d
4=
d 1/ 4, there is fillet air inlet conveying supervisor and aniseed cone cylinder admission line junction
r 1transition, there is fillet air inlet conveying arm and small powder cone cylinder admission line junction
r 2transition and
r 2=
r 1/ 2.
4. the speed change air-flow vortex kinetic energy pulping equipment of a kind of combined type feed liquid separation as claimed in claim 1, is characterized in that: described particle filter is the disc-shaped structure containing some filtration internal taper holes; Described filtration internal taper hole is the truncated cone-shaped structure of upper big, lower small, and upper bore dia is
Φ d 5and
Φ d 5=
Φ d 1/ 8, lower bore dia is
Φ d 6and
Φ d 6=
Φ d 1/ 24.
5. the speed change air-flow vortex kinetic energy pulping equipment of a kind of combined type feed liquid separation as claimed in claim 1, it is characterized in that: shown liquid slurry case is cuboid groove structure, liquid slurry case lid is rectangle structure, water inlet on liquid slurry case lid is grid-shaped structure, and be made up of 8 slots, the liquid slurry case lid draw-in groove on liquid slurry case lid often group is 4 and even circumferential circle distribution; Described pillar is 6, is distributed in cuboid groove bottom corner and middle part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520329288.7U CN204715117U (en) | 2015-05-21 | 2015-05-21 | The speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid is separated |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520329288.7U CN204715117U (en) | 2015-05-21 | 2015-05-21 | The speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid is separated |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204715117U true CN204715117U (en) | 2015-10-21 |
Family
ID=54314122
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520329288.7U Withdrawn - After Issue CN204715117U (en) | 2015-05-21 | 2015-05-21 | The speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid is separated |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204715117U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104831571A (en) * | 2015-05-21 | 2015-08-12 | 济南大学 | Combined liquid-material separation type variable-speed airflow eddy kinetic energy pulping device |
-
2015
- 2015-05-21 CN CN201520329288.7U patent/CN204715117U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104831571A (en) * | 2015-05-21 | 2015-08-12 | 济南大学 | Combined liquid-material separation type variable-speed airflow eddy kinetic energy pulping device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104532638B (en) | Drum cell body spiral backflows the vertical hydrabrusher of plate | |
| CN104233895B (en) | Up-flow pressure pulp screen | |
| CN107100024B (en) | D-shaped pulping equipment based on airflow vortex and stirring pulping | |
| CN104727173A (en) | Pulping device capable of achieving solid-liquid separation and secondary air vortex breakdown | |
| CN204715117U (en) | The speed change air-flow vortex kinetic energy pulping equipment that a kind of combined type feed liquid is separated | |
| CN104826745A (en) | Impeller of flotation machine | |
| CN104818635A (en) | Eddy kinetic energy gas flow material smashing and material-liquid separation pulping device | |
| CN104831571A (en) | Combined liquid-material separation type variable-speed airflow eddy kinetic energy pulping device | |
| CN204715116U (en) | The air-flow vortex kinetic energy pulping equipment that a kind of feed liquid is separated | |
| CN104818636B (en) | The air-flow vortex kinetic energy pulping equipment that a kind of feed liquid separates | |
| CN202155314U (en) | Centrifugal horizontal cage type powder separator with forced vortex | |
| CN201530946U (en) | Slurrying device for regenerating waste paper | |
| CN103253724A (en) | Rapid air dissolution device with micro-bubbles | |
| CN104878637A (en) | Vortex kinetic pulper | |
| CN102600995A (en) | Double-introduction-layer tower expanding cavity type separator | |
| CN204715119U (en) | A kind of take air as the coaxial reverse binary vortices kinetic energy pulp crushing apparatus of power | |
| CN204715118U (en) | A kind of based on three layers of air-flow vortex be stir power without rotor pulping equipment | |
| CN204570359U (en) | A kind of air-flow vortex kinetic energy pulper | |
| JPH02118190A (en) | Pulper | |
| CN104894905B (en) | A kind of is the pulping equipment without rotor stirring power based on three layers of air-flow vortex | |
| CN204570363U (en) | A kind of feed liquid is separated and the pulping equipment of auxiliary air vortex particle | |
| CN211134290U (en) | Rotary slurry separator | |
| CN205856909U (en) | A kind of Novel pulper sieve plate | |
| CN107398357A (en) | Horizontal type screw settling centrifuge charging cavity configuration | |
| CN204570362U (en) | A kind of high-efficiency pulper of partition type slurrying |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20151021 Effective date of abandoning: 20171114 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20151021 Effective date of abandoning: 20171114 |