CN204715115U - The pulping equipment that a kind of vortex kinetic energy airflow particle and feed liquid are separated - Google Patents
The pulping equipment that a kind of vortex kinetic energy airflow particle and feed liquid are separated Download PDFInfo
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- CN204715115U CN204715115U CN201520258194.5U CN201520258194U CN204715115U CN 204715115 U CN204715115 U CN 204715115U CN 201520258194 U CN201520258194 U CN 201520258194U CN 204715115 U CN204715115 U CN 204715115U
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- particle
- inner core
- urceolus
- vortex
- kinetic energy
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Abstract
The utility model provides a kind of vortex kinetic energy airflow particle and the pulping equipment of feed liquid separation, mainly comprises vortex crushed aggregates device and liquid slurry generating apparatus.Be characterized in that feed liquid is separated, first adopt vortex kinetic energy airflow and carry out particle, rear mixing with aqueous water generates slurries.The utility model is realized tangentially entering of gas by the admission line tangent with urceolus bottom outside edge and is formed circulation, realize in vortex particle district, increasing vortex kinetic energy by inner core, airflow stirring efficiency is improved in liquid material mixed zone, realize particle screening by internal taper hole and prevent blocking, by mixing and the stirring of particle carrier pipe realization material, liquid.
Description
Technical field
The utility model relates to a kind of vortex kinetic energy airflow particle and the pulping equipment of feed liquid separation, particularly relate to and a kind ofly realize tangentially entering of gas by the admission line tangent with urceolus bottom outside edge and form circulation, realize in vortex particle district, increasing vortex kinetic energy, in liquid material mixed zone, improving airflow stirring efficiency by inner core, realize particle screening by internal taper hole and prevent blocking, by mixing and the stirring of particle carrier pipe realization material, liquid, belong to the technical research field of paper-making industry pulping equipment.
Background technology
In paper manufacturing streams, need the pulpboard in water, waste and old books, waste carton etc. to be carried out size degradation to make paper pulp required in paper industry, and hydrabrusher is the modal equipment of this operation, waste material, by the motion of rotor, is made required unit for uniform suspension by this pulp crushing apparatus.But due to the unicity of current pulper working method and structure, cause following problem: one is that efficiency is low, the pulping of existing pulper is realized by the mechanical collision of feed liquid and rotor, bucket wall, and the power resources of collision are in the stirring of rotor to liquid material, this makes in the process of pulping, the energy ezpenditure of some, on the reactive loss of machinery, therefore causes the efficiency of machinery pulping very low; Two is that energy consumption is large, waste resource, and in the course of the work, not only want carry fluid to rotate, but also will overcome the resistance of fluid, this will consume a large amount of mechanical energy to pulp kneader rotor to a certain extent; In addition, for making the rotor motion resistance that particle is fully broken, reduction pulping causes, need a large amount of water, this also wastes a large amount of water resources to a certain extent.
Therefore, for the existing pulper problems such as in use ubiquitous efficiency is low, energy consumption is large, should consider from pulper working method and structure, design the high and a kind of pulping equipment that energy consumption is low of pulping efficiency.
Summary of the invention
The problems such as the efficiency that the utility model exists for existing pulping equipment is low, energy consumption is large, provide a kind of a kind of vortex kinetic energy airflow particle that can effectively solve the problem and the pulping equipment that is separated of feed liquid.
The pulping equipment that a kind of vortex kinetic energy airflow particle of the present utility model and feed liquid are separated is by the following technical solutions:
The pulping equipment that a kind of vortex kinetic energy airflow particle and feed liquid are separated, mainly comprise vortex crushed aggregates device and liquid slurry generating apparatus, described vortex crushed aggregates device is primarily of admission line, urceolus, inner core and particle filter composition, admission line is arranged on urceolus bottom outside edge place, inner tube installation is in urceolus, urceolus, inner core top is provided with top cover, the upper end of urceolus is had charging aperture and is sealed by feed cap, urceolus lower end is provided with outer pillar, urceolus, upper end between inner core is provided with particle filter, particle filter has internal taper hole, urceolus, inner core and particle filter surround vortex particle district, urceolus, inner core and top cover surround particle storage area, described liquid slurry generating apparatus forms primarily of inner core, particle carrier pipe and water inlet, inner core and top cover surround liquid material mixed zone, inner core is built with aqueous water, inner core bottom is provided with discharging opening, discharging opening surrounding is provided with interior pillar, particle carrier pipe is arranged on inner core upper end and is connected with particle storage area, and particle carrier pipe gos deep into inner core low side, and water inlet is opened at top cap central place.
Described admission line is arranged on urceolus bottom outside edge place, admission line and urceolus bottom outside edge tangent; Outer pillar bottom described urceolus, inner core and interior pillar are respectively 4, and are circumferentially uniformly distributed.
Described urceolus, inner core are an entirety, and urceolus is cylindrical structural, and inner core is the truncated cone-shaped structure of upper big, lower small, and the bottom outside inner core angularly
α, angle
αoptimized scope be 45 degree ~ 60 degree.
Described particle filter is cirque structure, and particle filter has some internal taper holes, and internal taper hole is big end down truncated cone-shaped structure, and in certain taper, optimum range of taper is 1:3 ~ 1:2.
Described particle carrier pipe is pipe, and internal diameter is 4 ~ 6 times of internal taper hole path, and aqueous water is equipped with in lower end, liquid material mixed zone, and the water yield can be determined according to inlet amount and liquid slurry concentration.
Admission line is arranged on urceolus bottom outside edge and tangent with lateral border by the utility model, tangentially entering and forming circulation of gas can be realized by this design, namely when compressed air enters into admission line, because of admission line and lateral border tangent, can make air under the effect of inertia, rotating along outer tube inner wall with the state of minimum energy loss, and form eddy current in vortex particle district, carrying out for realizing vortex kinetic energy airflow the source of the gas that particle provides abundance; Outer pillar, interior pillar design are 4 and are circumferentially uniformly distributed, can be by this design the stability that whole pulping equipment provides support and maintenance equipment runs, what produce during abatement apparatus runs rocks.
Urceolus, inner core are designed to an entirety by the utility model, pulping equipment both can have been made compact, and can increase Whole Equipment intensity again by this design; Urceolus is designed to cylindrical structural, and this design can make gas in vortex particle district form circulation, eliminates eddy airstream because of partial structurtes to suddenly change the kinetic energy loss caused; Inner core is designed to the truncated cone-shaped structure of upper big, lower small, the bottom outside inner core angularly
αhad the following advantages by this design: one is the acceleration realizing air-flow in vortex particle district, thus improve the kinetic energy of eddy airstream, increase its crushing force to particle, after namely Compressed Gas enters vortex particle district, along with the sectional area in vortex particle district reduces gradually, speed constantly increases, and impels the kinetic energy of eddy airstream to increase gradually, thus the particle under vortex is driven has larger kinetic energy when mutually colliding, fragmentation is more thorough, produces less particle particle; Two is the liquid slurries realizing generating in liquid material mixed zone even concentration, namely under gravity, larger particle particle will concentrate on the bottom of inner core, by particle carrier pipe inner high voltage air-flow to particle granule impact, float making the particle particle being deposited on bottom, and being designed to the long-pending bottom of small cross sections, object, for reducing high pressure draught shock zone, improves airflow stirring efficiency.
Internal taper hole in particle filter is designed to big end down truncated cone-shaped structure by the utility model, by this design, there is following effect: one be to fragmentation after particle screen, only have more short grained particle can enter particle storage area, ensure the even particle size of liquid slurry, two is prevent larger Particle Blocking round platform hole, if larger particle particle enters into round platform hole, along with eddy flow at round platform upper surface through forming certain back pressure later, back pressure will produce suction, and big end down this structure can by the sucking-off easily of increasing particle particle.
The internal diameter of particle carrier pipe is designed to 4 ~ 6 times of internal taper hole path by the utility model, by this design, can prevent particle from elongated particle carrier pipe, producing blocking; Be deep in bottom aqueous water by particle carrier pipe, this design can realize being moved by bottom belt hydrodynamic, material by high pressure draught, plays the effect of stirring liquid slurry.
The beneficial effects of the utility model are: realized tangentially entering of gas by the admission line tangent with urceolus bottom outside edge and formed circulation; Vortex kinetic energy loss is eliminated by cylindrical outer barrel; Realize eddy airstream by the truncated cone-shaped inner core of upper big, lower small to accelerate, increase vortex kinetic energy, and realize reducing high pressure draught shock zone, improve airflow stirring efficiency; Realize particle screening by big end down truncated cone-shaped internal taper hole and prevent blocking; Realize preventing particle from blocking by the particle carrier pipe of 4 ~ 6 times of internal taper hole paths; Be deep into bottom aqueous water by particle carrier pipe and realize stirring liquid slurry.
Accompanying drawing explanation
Fig. 1 is overall structure schematic front view of the present utility model.
Fig. 2 is overall structure schematic top plan view of the present utility model.
Fig. 3 is the partial schematic diagram of the utility model particle filter and charging protective cover.
Wherein: 1, discharging opening, 2, interior pillar, 3, outer pillar, 4, admission line, 5, urceolus, 6, vortex particle district, 7, feed cap, 8, particle filter, 9, internal taper hole, 10, particle storage area, 11, particle carrier pipe, 12, liquid material mixed zone, 13 water inlets, 14, aqueous water, 15, inner core, 16 top covers.
Detailed description of the invention
Embodiment:
As shown in Figure 1, Figure 2 and Figure 3, the pulping equipment that a kind of vortex kinetic energy airflow particle of the present utility model and feed liquid are separated, mainly comprises vortex crushed aggregates device and liquid slurry generating apparatus.Vortex crushed aggregates device forms primarily of admission line 4, urceolus 5, inner core 15 and particle filter 8, admission line 4 is arranged on urceolus 5 bottom outside edge and tangent with lateral border, this structure can realize tangentially entering and forming circulation of gas, namely when compressed air enters into admission line 4, because admission line 4 and urceolus 5 lateral border are tangent, can make gas under the effect of inertia, rotate along urceolus 5 inwall with the state of minimum energy loss, and eddy current is formed in vortex particle district 6, carry out for realizing vortex kinetic energy airflow the source of the gas that particle provides abundance.
Urceolus 5, inner core 15 are designed to an entirety, and this design both can make pulping equipment compact, can increase Whole Equipment intensity again; Urceolus 5 is designed to cylindrical structural, and this design can make gas in vortex particle district 6 form circulation, eliminates eddy airstream because of partial structurtes to suddenly change the kinetic energy loss caused.
Inner core 15 is arranged in urceolus 5, and inner core 15 is designed to the truncated cone-shaped structure of upper big, lower small, and the bottom outside inner core 15 angularly
α, angle
αoptimized scope be 45 degree ~ 60 degree, this design is when equipment runs, one is the acceleration realizing air-flow in vortex particle district 6, thus improve the kinetic energy of eddy airstream, increase its crushing force to particle, namely after Compressed Gas enters vortex particle district 6, along with the sectional area in vortex particle district 6 reduces gradually, speed constantly increases, the kinetic energy of eddy airstream is impelled to increase gradually, thus the particle under making vortex drive has larger kinetic energy when mutually colliding, fragmentation is more thorough, produces less particle particle; Two is the liquid slurries realizing generating in liquid material mixed zone 12 even concentration, namely under gravity, larger particle particle will concentrate on the bottom of inner core 15, by particle carrier pipe 11 inner high voltage air-flow to particle granule impact, float making the particle particle being deposited on bottom, and being designed to the long-pending bottom of small cross sections, object, for reducing high pressure draught shock zone, improves airflow stirring efficiency.
Urceolus 5, inner core 15 top are provided with top cover 16, and the upper end of urceolus 5 is had charging aperture and sealed by feed cap 7, and urceolus 5 lower end is provided with outer pillar 3, and inner core 15 lower end is provided with interior pillar 2; Outer pillar 3 and interior pillar 2 are respectively 4, and are circumferentially uniformly distributed, 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.
Upper end between urceolus 5, inner core 15 is provided with particle filter 8, particle filter 8 is cirque structure, particle filter 8 has internal taper hole 9, internal taper hole 9 is big end down truncated cone-shaped structure, and in certain taper, optimum range of taper is 1:3 ~ 1:2, this design is when equipment works, one is realize screening the particle after fragmentation, only has more short grained particle can enter particle storage area 10, ensures the even particle size of liquid slurry; Two is prevent larger Particle Blocking round platform hole, if larger particle particle enters into round platform hole, along with eddy flow at round platform upper surface through forming certain back pressure later, back pressure will produce suction, and big end down this structure can strengthen particle particle sucking-off easily.Urceolus 5, inner core 15 and particle filter 8 surround vortex particle district 6, and urceolus 5, inner core 15 and top cover 16 surround particle storage area 10.
Liquid slurry generating apparatus forms primarily of inner core 5, particle carrier pipe 11 and water inlet 13, inner core 5 and top cover 16 surround liquid material mixed zone 12, inner core 5 is built with aqueous water 14, inner core 5 bottom is provided with discharging opening 1, particle carrier pipe 11 is arranged on inner core 5 upper end and is connected with particle storage area 10, particle carrier pipe 11 gos deep into inner core 15 low side, and water inlet 13 is opened in top cover 16 center.Particle carrier pipe 11 is pipe, and internal diameter is 4 ~ 6 times of internal taper hole 9 path, and this design can prevent particle from elongated particle carrier pipe 11, producing blocking; Particle carrier pipe 11 is deep in bottom aqueous water 14, and this design can realize being moved by bottom belt hydrodynamic, material by high pressure draught, plays the effect of stirring liquid slurry.In liquid material mixed zone 12, the water yield of aqueous water can be determined according to inlet amount and liquid slurry concentration.
Claims (5)
1. the pulping equipment that is separated of a vortex kinetic energy airflow particle and feed liquid, mainly comprise vortex crushed aggregates device and liquid slurry generating apparatus, it is characterized in that: described vortex crushed aggregates device is primarily of admission line, urceolus, inner core and particle filter composition, admission line is arranged on urceolus bottom outside edge place, inner tube installation is in urceolus, urceolus, inner core top is provided with top cover, the upper end of urceolus is had charging aperture and is sealed by feed cap, urceolus lower end is provided with outer pillar, urceolus, upper end between inner core is provided with particle filter, particle filter has internal taper hole, urceolus, inner core and particle filter surround vortex particle district, urceolus, inner core and top cover surround particle storage area, described liquid slurry generating apparatus forms primarily of inner core, particle carrier pipe and water inlet, inner core and top cover surround liquid material mixed zone, inner core is built with aqueous water, inner core bottom is provided with discharging opening, discharging opening surrounding is provided with interior pillar, particle carrier pipe is arranged on inner core upper end and is connected with particle storage area, and particle carrier pipe gos deep into inner core low side, and water inlet is opened at top cap central place.
2. the pulping equipment that is separated of a kind of vortex kinetic energy airflow particle as claimed in claim 1 and feed liquid, is characterized in that: described admission line is arranged on urceolus bottom outside edge place, admission line and urceolus bottom outside edge tangent; Outer pillar bottom described urceolus, inner core and interior pillar are respectively 4, and are circumferentially uniformly distributed.
3. the pulping equipment that is separated of a kind of vortex kinetic energy airflow particle as claimed in claim 1 and feed liquid, it is characterized in that: described urceolus, inner core are an entirety, urceolus is cylindrical structural, and inner core is the truncated cone-shaped structure of upper big, lower small, and the bottom outside inner core angularly
α,
αthe optimized scope of angle is 45 degree ~ 60 degree.
4. the pulping equipment that is separated of a kind of vortex kinetic energy airflow particle as claimed in claim 1 and feed liquid, it is characterized in that: described particle filter is cirque structure, particle filter has some internal taper holes, internal taper hole is big end down truncated cone-shaped structure, in certain taper, optimum range of taper is 1:3 ~ 1:2.
5. the pulping equipment that is separated of a kind of vortex kinetic energy airflow particle as claimed in claim 1 and feed liquid, it is characterized in that: described particle carrier pipe is pipe, internal diameter is 4 ~ 6 times of internal taper hole path, and aqueous water is equipped with in lower end, liquid material mixed zone, and the water yield can be determined according to inlet amount and liquid slurry concentration.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520258194.5U CN204715115U (en) | 2015-04-27 | 2015-04-27 | The pulping equipment that a kind of vortex kinetic energy airflow particle and feed liquid are separated |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520258194.5U CN204715115U (en) | 2015-04-27 | 2015-04-27 | The pulping equipment that a kind of vortex kinetic energy airflow particle and feed liquid are separated |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204715115U true CN204715115U (en) | 2015-10-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520258194.5U Withdrawn - After Issue CN204715115U (en) | 2015-04-27 | 2015-04-27 | The pulping equipment that a kind of vortex kinetic energy airflow particle and feed liquid are separated |
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| Country | Link |
|---|---|
| CN (1) | CN204715115U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104818635A (en) * | 2015-04-27 | 2015-08-05 | 济南大学 | Eddy kinetic energy gas flow material smashing and material-liquid separation pulping device |
| CN107841898A (en) * | 2017-12-07 | 2018-03-27 | 福建省联盛纸业有限责任公司 | A kind of paper machine paper slag grading plant |
-
2015
- 2015-04-27 CN CN201520258194.5U patent/CN204715115U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104818635A (en) * | 2015-04-27 | 2015-08-05 | 济南大学 | Eddy kinetic energy gas flow material smashing and material-liquid separation pulping device |
| CN104818635B (en) * | 2015-04-27 | 2016-08-17 | 济南大学 | The pulping equipment that a kind of vortex kinetic energy airflow particle and feed liquid separate |
| CN107841898A (en) * | 2017-12-07 | 2018-03-27 | 福建省联盛纸业有限责任公司 | A kind of paper machine paper slag grading plant |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20151021 Effective date of abandoning: 20160817 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20151021 Effective date of abandoning: 20160817 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |