CN103338867B - Classification device, and classification method, blast machining device provided with this classification device, and blast machining method - Google Patents
Classification device, and classification method, blast machining device provided with this classification device, and blast machining method Download PDFInfo
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- CN103338867B CN103338867B CN201280007188.1A CN201280007188A CN103338867B CN 103338867 B CN103338867 B CN 103338867B CN 201280007188 A CN201280007188 A CN 201280007188A CN 103338867 B CN103338867 B CN 103338867B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C9/00—Appurtenances of abrasive blasting machines or devices, e.g. working chambers, arrangements for handling used abrasive material
- B24C9/006—Treatment of used abrasive material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/62—Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type
- B03B5/64—Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type of the free settling type
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
- B03B5/62—Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type
- B03B5/623—Upward current classifiers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D3/00—Differential sedimentation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C9/00—Appurtenances of abrasive blasting machines or devices, e.g. working chambers, arrangements for handling used abrasive material
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Abstract
A classification device for classifying particles dispersed in a slurry, using the difference in precipitation speed, and a blast machining device provided with this device are provided. The classification device is provided with a casing for introducing a slurry and classifying large-diameter particles and small-diameter particles, and a slurry introduction mechanism for introducing the slurry. The casing is partitioned into a slurry introduction chamber, a first recovery chamber, and a second recovery chamber, by a slurry introduction member and a classification member erectly disposed from the bottom surface of the classification chamber main body. This classification device can be used as a sorting mechanism for sorting particles in a slurry into abrasive particles that can be used again and particles that cannot, in a wet blast machining device.
Description
Technical field
The present invention relates to the wet classification device for carrying out classification to the particle be scattered in liquid with the size of regulation.
Background technology
In the blasting apparatus etc. of wet type, the device (such as Japanese Unexamined Patent Publication 2005-335044 publication) of sorting is carried out in extensive use to the solids be scattered in slip with the size of regulation.As this device, be known to use Cyclonic separating apparatus or filter cloth, net and so on the method for the filter of the size openings of regulation, the sedimentation method for separating using continuous sedimentation thickener etc.For using the separation carried out of filter, to there is by using for a long time opening portion by the problem of Particles Blocking.For sedimentation separation, to sedimentation, need a large amount of time and be only applicable to heavy particle.As other method, such as, in Japanese Unexamined Patent Publication 10-066895 publication and Japanese Unexamined Patent Publication 2000-005626 publication, disclose the separator of combination waterpower and sedimentation separation.
In No. 10-066895, Japanese Unexamined Patent Publication, make slip with from the inflow entrance on separation chamber top by the first separation chamber, the second separation chamber flowing into abreast from the mode that flow export is discharged, and in order to be separated from oversize grain by minuteness particle, the liquid of the bottom of the second separation chamber is flowed via pump.There is lighter particle owing to piling up in the bottom of the second separation chamber, therefore exist and cause towards the blocked misgivings in the path of pump because of the particle of sedimentation.Further, owing to needing above-mentioned pump, therefore device becomes complicated.In patent document 3, water is flowed into from the bottom of separation tube, and drop into as the particle being sorted thing from the top of this separation tube.Heavy particle is settled down to the bottom of this separation tube, and lepton is discharged by from this separation tube together with the water of spilling (overflow).Therefore, device self becomes large, needs to change separation tube self to change the size, the classification point that are sorted thing.
Summary of the invention
In the present invention, provide a kind of can simply to construct blasting apparatus and the method for blasting of the wet type of carrying out the grading plant of the wet type of classification and stage division to the solids in slip accurately and possess this grading plant.
Technical scheme 1 of the present invention relates to a kind of grading plant, this grading plant is for utilizing the difference of sinking speed to carry out the device of classification to the solids be dispersed in slip, the feature of above-mentioned grading plant is, above-mentioned grading plant possesses: framework, above-mentioned slip is imported this framework, and this framework is used for above-mentioned slip to be classified into major diameter particle and minor diameter particle, and slip introducing mechanism, this slip introducing mechanism is used for slip to import above-mentioned framework, for above-mentioned framework, be separated into the first recovery room and second by the classification parts of tabular in this framework and reclaim room, above-mentioned classification parts erect setting from the bottom surface of above-mentioned framework, and there is the front end being provided with gap between the end face of above-mentioned framework, reclaim indoor above-mentioned first and be formed with slip importing room, the sidewall of this slip importing room is erected the slip introduction part of the tabular of setting by the bottom surface of reclaiming room from above-mentioned first, or above-mentioned slip introduction part and above-mentioned first reclaims the wall formation of room, the lower end importing room at above-mentioned slip is formed with the slip introducing port linked with above-mentioned slip introducing mechanism, and, above-mentioned slip imports the open upper end of room.
And, technical scheme 2 of the present invention relates to a kind of grading plant, this grading plant is for utilizing the difference of sinking speed to carry out the device of classification to the solids be dispersed in slip, the feature of above-mentioned grading plant is, above-mentioned grading plant possesses: framework, above-mentioned slip is imported this framework, and this framework is used for above-mentioned slip to be classified into major diameter particle and minor diameter particle, and slip introducing mechanism, this slip introducing mechanism is used for slip to import above-mentioned framework, for above-mentioned framework, be separated into the first recovery room and second by the classification parts of tabular in this framework and reclaim room, above-mentioned classification parts erect setting from the bottom surface of above-mentioned framework, and there is multiple opening portion that can block, reclaim indoor above-mentioned first and be formed with slip importing room, the sidewall of this slip importing room is erected the slip introduction part of the tabular of setting by the bottom surface of reclaiming room from above-mentioned first, or above-mentioned slip introduction part and above-mentioned first reclaims the wall formation of room, the lower end importing room at above-mentioned slip is formed with the slip introducing port linked with above-mentioned slip introducing mechanism, and, above-mentioned slip imports the open upper end of room.It is characterized in that the slip utilizing slip introduction part to form open upper end imports room.The bottom that room is reclaimed in the room heavier major diameter particle precipitation to the first be fed to the slip of the first recovery room is imported from slip.On the other hand, lighter minor diameter particle reclaims room by the gap between above-mentioned classification parts and above-mentioned top or the opening portion that is arranged at above-mentioned classification parts towards second and moves.
The feature of technical scheme 3 is, in the grading plant described in technical scheme 1 or 2, and can loading and unloading at least partially of above-mentioned classification parts.By the change height at least partially of handling classification parts, can change and reclaim in the first recovery room and second particle diameter reclaimed room.
The feature of technical scheme 4 is, in the grading plant described in any one in technical scheme 1 to 3, above-mentioned slip imports room and is formed as the sectional area expansion along with trend top.The solids existed in slip condense and form the situation of offspring.Offspring will cause effectiveness of classification to reduce.By being formed as structure of the present invention, when being imported room by slip, offspring fragmentation can be formed as primary particle.In addition, so-called " along with trend top, sectional area expands " not only comprises situation about expanding continuously, the concept also comprising the situation that an only part expands.Such as, the structure continuously near upper end with identical sectional area can be formed as.Further, after be about to describe, also can along with trend above and make sectional area expand after near upper end, make reduced cross-sectional area.
The feature of the invention of technical scheme 5 and 6 is, in grading plant described any one of technical scheme 1 to 4, possesses the acceleration mechanism for accelerating slip in the upper end of above-mentioned slip importing room.Risen by speed when making the upper end by above-mentioned slip importing room, can effectiveness of classification be improved.
The feature of the invention of technical scheme 7 and 8 is, in the grading plant described in the invention of technical scheme 5 or 6, utilizes above-mentioned acceleration mechanism that the sectional area of above-mentioned slip introduction part is reduced gradually along with trend top.According to the present invention, simple structure can be utilized to accelerate the speed of the slip being imported the upper end of room by slip.
The feature of the invention of technical scheme 9 is, in grading plant described any one of technical scheme 1 to 8, above-mentioned slip introducing mechanism possesses the hoisting mechanism for promoting slip, is configured with the boot speed guiding mechanism of the boot speed for adjusting above-mentioned slip between above-mentioned slip introducing port and above-mentioned hoisting mechanism.The speed of the slip be imported into from slip introducing port by adjustment, can carry out the fine setting of classification point.
Technical scheme 10 relates to a kind of blasting apparatus, this blasting apparatus is for being sprayed towards machined object with the blasting apparatus carrying out shot-peening processing together with gases at high pressure by the slip being dispersed with abrasive particle in a liquid, the feature of above-mentioned blasting apparatus is, above-mentioned blasting apparatus possesses: shot-peening Processing Room, is configured with nozzle in the inside of this shot-peening Processing Room; Slurry vessel, this slurry vessel is for storing above-mentioned slip; Sorting mechanism, this sorting mechanism is used for carrying out classification to the particle in the slip in above-mentioned slurry vessel; And separating mechanism, this separating mechanism is used for carrying out Separation of Solid and Liquid to the slip comprising the minor diameter particle after by above-mentioned grading plant classification, and above-mentioned sorting mechanism is grading plant described any one of technical scheme 1 to 9.Grading plant of the present invention can be adapted at can again using with the sorting mechanism becoming the abrasive particle of size and the cutting particle of machined object that are not suitable for shot-peening processing for the abrasive particle of shot-peening processing as sorting in the blasting apparatus of wet type.
The feature of the invention involved by technical scheme 11 is, in the blasting apparatus described in technical scheme 10, above-mentioned separating mechanism is magnetic force sorting device.Under abrasive particle and the magnetic situation of machined object tool, magnetic grader can be utilized easily to carry out Separation of Solid and Liquid.
The feature of the invention involved by technical scheme 12 is, in the blasting apparatus described in technical scheme 10 or 11, in above-mentioned shot-peening Processing Room, be configured with the cleaning nozzle for cleaning the machined object after shot-peening processing, above-mentioned cleaning nozzle sprays the liquid gone out by above-mentioned its disengagement.Machined object after shot-peening process finishing is attached with the cutting particle etc. of abrasive particle, machined object, needs to clean, and as cleansing medium, can use the liquid of solid-liquid separation.
Technical scheme 13 relates to a kind of stage division, it is characterized in that, this stage division is grading plant described any one of operation technique scheme 1 to 12 carries out classification stage division to the solids be dispersed in slip, comprising: above-mentioned slip is imported above-mentioned slip from above-mentioned slip introducing port and imports indoor operation; The opening portion making be imported into above-mentioned slip import the upper end of room from above-mentioned slip is spread and the operation of discharging; Make the minor diameter particle in the solids in above-mentioned slip reclaim indoor moving by the gap between above-mentioned classification parts and above-mentioned top or the opening portion being arranged at above-mentioned classification parts towards above-mentioned second, and make the major diameter particle precipitation in the solids in above-mentioned slip reclaim the operation of the bottom of room to above-mentioned first; And make the above-mentioned minor diameter particle precipitation after moving to above-mentioned second recovery indoor to the operation of the bottom of this second recovery room.Import room from slip to spread and the heavier major diameter particle of weight ratio solids after being discharged can not move to the second recovery room and be settled down to the bottom of the first recovery room.On the other hand, the minor diameter particle that weight ratio is lighter moves to the second recovery room and is settled down to the bottom of the second recovery room.In addition, can only be undertaken by the deadweight of solids towards the first sedimentation of reclaiming the bottom of room and the second recovery room, also can combine with the expulsion force from the opening portion being arranged on respective bottom and carry out, can be any one.
The feature of the invention described in technical scheme 14 is, in the stage division described in technical scheme 13, changed the diameter of the solids reclaiming room movement towards above-mentioned second by the distance changed between the lower end of distance between the upper end of above-mentioned classification parts and above-mentioned top or above-mentioned opening portion and above-mentioned top.By adjusting the distance between the upper end of the height from bottom surface, i.e. the classification parts of above-mentioned classification parts and the top of framework, the diameter of the solids reclaiming room movement towards second can be changed.That is, classification point can be changed.Such as, by reducing above-mentioned height, become large, therefore, it is possible to improve classification point towards the second diameter reclaiming the solids of room movement.
Technical scheme 15 and 16 relates to a kind of stage division, it is characterized in that, this stage division is grading plant described in operation technique scheme 5 or 6 carries out classification stage division to the solids be dispersed in slip, comprising: above-mentioned slip is imported above-mentioned slip from above-mentioned slip introducing port and imports indoor operation; Utilize above-mentioned acceleration mechanism to accelerate the above-mentioned slip be imported into, and the opening portion making above-mentioned slip import the upper end of room from above-mentioned slip is spread and the operation of discharging; Make the minor diameter particle in the solids in above-mentioned slip reclaim indoor moving by the gap between above-mentioned classification parts and above-mentioned top or the opening portion being arranged at above-mentioned classification parts towards above-mentioned second, and make the major diameter particle precipitation in the solids in above-mentioned slip reclaim the operation of the bottom of room to above-mentioned first; And make the above-mentioned minor diameter particle precipitation after moving to above-mentioned second recovery indoor to the operation of the bottom of this second recovery room.By making the speed of slip rise, minor diameter particle can be made not to be trapped in the first recovery room and to move towards the second recovery room.As a result, can effectiveness of classification be improved, or make classification point increase.
Technical scheme 17 relates to a kind of stage division, it is characterized in that, this stage division is grading plant described in operation technique scheme 9 carries out classification stage division to the solids be dispersed in slip, is changed the diameter of the solids reclaiming room movement towards above-mentioned second by the boot speed of the slip changing above-mentioned boot speed guiding mechanism place.By the boot speed utilizing above-mentioned boot speed guiding mechanism to change slip, classification point easily can be adjusted.
Technical scheme 18 relates to a kind of method for blasting, it is characterized in that, this method for blasting is the method for blasting that blasting apparatus described any one of operation technique scheme 10 to 12 carries out, and comprising: in above-mentioned slurry vessel, drop into liquid and abrasive particle and make it to disperse and obtain the operation of slip; By the slurry pipeline transport in above-mentioned slurry vessel to said nozzle, and mix with gases at high pressure and utilize the operation that said nozzle sprays towards machined object; The cutting particle of sprayed slip and machined object is stored in the operation of slurry vessel; By the slurry pipeline transport of above-mentioned slurry vessel to the operation of above-mentioned sorting mechanism; The operation of slurry vessel is again delivered to as the solids being used for carrying out shot-peening processing using reclaiming in room above-mentioned first the major diameter particle that is recovered to; And reclaim above-mentioned second the operation that the minor diameter particle that is recovered to of room reclaims as deposit.According to the present invention, the solids in slip can be separated into be applicable to again carry out shot-peening processing abrasive particle and be not suitable for shot-peening processing the abrasive particle of size and the cutting particle of machined object.
Technical scheme 19 relates to a kind of method for blasting, it is characterized in that, this method for blasting is the method for blasting that the blasting apparatus described in operation technique scheme 11 carries out, and comprising: in above-mentioned slurry vessel, drop into liquid and the magnetic abrasive particle of tool and make it to disperse and obtain the operation of slip; By the slurry pipeline transport in above-mentioned slurry vessel to said nozzle, and mix with gases at high pressure and utilize the operation that said nozzle sprays towards the magnetic machined object of tool; The cutting particle of sprayed slip and machined object is stored in the operation of slurry vessel; By the slurry pipeline transport of above-mentioned slurry vessel to the operation of above-mentioned sorting mechanism; The operation of slurry vessel is again delivered to as the solids being used for carrying out shot-peening processing using reclaiming in room above-mentioned first the major diameter particle that is recovered to; The operation of slurry pipeline transport to above-mentioned magnetic force sorting device that above-mentioned second reclaims the minor diameter particle that room is recovered to will be included in; And utilize magnetic force to carry out the operation of Separation of Solid and Liquid to the slip being delivered to above-mentioned magnetic force sorting device.When under abrasive particle and the magnetic situation of machined object tool, easily can carry out Separation of Solid and Liquid to being included in the above-mentioned second slip reclaiming the minor diameter particle (being namely not suitable for the abrasive particle of size and the cutting particle of machined object of shot-peening processing) reclaimed room, and above-mentioned minor diameter particle is reclaimed as deposit.
Technical scheme 20 relates to a kind of grading plant, this grading plant is for utilizing the difference of sinking speed to carry out the grading plant of classification to the solids be dispersed in slip, the feature of above-mentioned grading plant is, above-mentioned grading plant possesses: the framework of tubular, above-mentioned slip is imported this framework, and this framework is used for above-mentioned slip to be classified into major diameter particle and minor diameter particle; And slip introducing mechanism, this slip introducing mechanism is for importing above-mentioned slip, above-mentioned framework possesses: the classification parts of tabular, these classification parts erect setting from the bottom surface of above-mentioned framework in the mode being provided with gap between the end face of above-mentioned framework, and above-mentioned framework are separated into the first recovery room being formed with major diameter particle outlet in bottom surface and the second recovery room being formed with minor diameter particle outlet in bottom surface; And the slip introduction part of tabular, this slip introduction part configures upward from the above-mentioned first bottom surface of reclaiming between the slip introducing port of the bottom surface opening of room and above-mentioned major diameter particle outlet, spread upward for making to be fed to the above-mentioned first slip reclaiming indoor from above-mentioned slip introducing port, above-mentioned slip introducing mechanism one end is communicated with above-mentioned slip introducing port, the other end is communicated with hoisting mechanism.According to the present invention, can provide can simply to construct the device carrying out classification accurately.
The present invention can provide simple structure and the high grading plant of effectiveness of classification and stage division.
Further, for grading plant of the present invention, the difference in specific gravity of major diameter particle and minor diameter particle is larger, more can carry out classification efficiently.For the classification of the slip in the blasting apparatus of wet type, due to minor diameter particle be the machined object produced by shot-peening processing cutting particle and by colliding with machined object breakage, breach etc. thus become the abrasive particle of the size being not suitable for reusing, the difference in specific gravity therefore and between major diameter particle that is the abrasive particle that can reuse is large.Therefore, it is possible to suitably apply grading plant of the present invention.
The diameter of solids of classification and proportion can there is no particular determination in the present invention, but the difference in specific gravity of major diameter particle and minor diameter particle and particle diameter difference more can carry out classification more greatly accurately.Further, although the difference in specific gravity of major diameter particle and minor diameter particle and particle diameter difference large, for relative to the slip S with wide size distribution, as long as classification o'clock is the scope of 100 ~ 1000 μm, just can carry out classification good especially.
The Japanese Patent Application 2011-123863 publication that the application filed an application in Japan based on June 2nd, 2011 and No. 2012-051173, the Japanese Patent Application of filing an application on March 8th, 2012, its content all as the application content and form a application's part.
Further, the present invention can be understood more completely according to following detailed description.But detailed description and specific embodiment are the preferred embodiment of the present invention, and the object being only used for illustrating is recorded.Those skilled in the art can know various change, change according to this detailed description.
Applicant is not intended any one in described embodiment to be dedicated to the public, even if disclosed change, the scheme be not contained on language in the scope of claim in replacement scheme, is under the jurisdiction of a part for invention at the theory of identity nextpage.
In the record of this description or claims, for the use of noun and identical deictic word, as long as there is no specially instruction or negate clearly then should be interpreted as comprising odd number and plural both sides according to the syntax.The use of the arbitrary example provided in this manual or exemplary language (such as " etc. ") also only intention be easy to that the present invention will be described, as long as be not specially recorded in claim, then scope of the present invention can not apply restriction.
Accompanying drawing explanation
Fig. 1 is the key diagram for illustration of the grading plant in present embodiment.(A) of Fig. 1 is the schematic diagram that longitudinal section is shown, (B) of Fig. 1 is along the sectional view of the A-A line in Fig. 1 (A).
Fig. 2 is the key diagram of modification importing room for illustration of the slip of present embodiment.
Fig. 3 is the key diagram of the acceleration mechanism for illustration of present embodiment.
Fig. 4 is the key diagram of the structure of blasting apparatus for illustration of the wet type in present embodiment.
Fig. 5 is the key diagram of the modification of the blasting apparatus of wet type for illustration of present embodiment.
Detailed description of the invention
Be described for the situation of grading plant of the present invention and the blasting apparatus that this grading plant is applied to wet type.In addition, grading plant of the present invention is not limited to the mode described in embodiment, can suitably change as required.Further, for the left and right above-below direction that present embodiment is recorded, as long as specially do not explain, the direction in the figure just referred to.
(grading plant)
First, grading plant is described.Grading plant 10 comprises framework 11 and slip introducing mechanism 17.As shown in (A) of Fig. 1, framework 1 for cross section be the tubular of quadrangle, and top (topmost in this figure) is blocked by top board.In bottom, offer slip introducing port 12a, major diameter particle outlet 13a, minor diameter particle outlet 14a successively according to the order from the left side of this figure.
In the middle of both major diameter particle outlet 13a and minor diameter particle outlet 14a, erect in the bottom of framework 11 and be provided with classification parts 16, the space of framework 11 inside is separated into the second recovery room 14 that first of the upstream side of the stream of slip reclaims the downstream of the stream of room 13 and slip by these classification parts 16.These classification parts 16 in tabular, and configure in the mode being formed with gap between upper end and the top of framework 11.
Near slip introducing port 12a, be configured with upward slip introduction part 15 from the bottom of framework.Slip introduction part 15 is in tabular, and the height and position (above-below direction at (A) of Fig. 1) of upper end is lower than the height and position of above-mentioned classification parts 16 upper end.Further, slip introduction part 15 configures in the mode of surrounding slip introducing port, is separated out slip imports room 12 in the first space of reclaiming inside, room 13.In the present embodiment, as shown in (B) of Fig. 1, the sidewall formation of the framework 11 of the slip introduction part 15 being configured in three directions (top in this figure, below, right) and the left direction being positioned at this figure is utilized to comprise space that is the slip importing room 12 of slip introducing port 12a.In addition, as long as can form this space, direction, the shape of configuration slip introduction part 15 there is no particular determination.Such as, also three directions (top of this figure, below, left) can be made to be the wall of the first recovery room 13, only make a remaining wall (right of this figure) for slip introduction part 15 ((A) with reference to Fig. 2), further, also can be made up of the slip introduction part 15 being configured in four direction (top, below, left, right) ((B) with reference to Fig. 2).And, the cross section (cross section of the paper vertical direction in (A) of Fig. 1) that slip imports room 12 is not limited to the such quadrangle of embodiment, also can be such as the semi-circular shape ((C) with reference to Fig. 2) utilizing the slip introduction part 15 of drum and the sidewall of framework 11 to be formed, also can be the toroidal ((D) with reference to Fig. 2) only formed by the slip introduction part 15 of drum.
As mentioned above, the space of framework 11 inside is separated by slip introduction part 15 and classification parts 16.Thus, from left side starts, be formed with the space comprising slip introducing port 12a that is slip successively import room 12, comprise slip and import the space that is first of room 12 and major diameter particle outlet 13a and reclaim room 13 and room 14 is reclaimed in the space that is second comprising minor diameter particle outlet 14a.
The valve of guiding mechanism that is major diameter particle dump valve and minor diameter particle dump valve (not shown) that possess blocking and flow is preferably linked with respectively at above-mentioned major diameter particle outlet 13a and minor diameter particle outlet 14a.Before classification starts, major diameter particle dump valve and minor diameter particle dump valve are all closed.
Slip introducing mechanism 17 is linked with at above-mentioned slip introducing port 12a.Slip introducing mechanism 17 comprises hoisting mechanism (shielding electrodynamic pump) and pipe H1.Pipe H1 is utilized to link above-mentioned hoisting mechanism 17 and slip introducing port 12a.Further, be linked with pipe H2 at above-mentioned hoisting mechanism P1, utilize pipe H2 to link above-mentioned hoisting mechanism 17 and slurry vessel 22.
Further, the slip of the solids be dispersed with in a liquid for carrying out classification is dropped into slurry vessel 12.Preferably be configured with rabbling mechanism (not shown) at slurry vessel, in order to avoid the solids in slip S are piled up in bottom.For rabbling mechanism, stirring vane can be utilized to stir slip, current can be utilized to stir slip, and pump etc. can be utilized to make slurry circulation and stir, and can be any one, and, also suitably can select other known method.
Secondly, by making hoisting mechanism P1 work, slip S is imported in framework 11 from above-mentioned slip introducing port 12a.The flow velocity of slip S has to be elected solids as and can not import sedimentation in room 12 at slip and the 0.5 ~ 5m/s that can not impact classification.
For the slip S be imported into from slip introducing port 12a, solids condense each other and form agglomerate (offspring) sometimes.Grading plant of the present invention is that the difference of the sinking speed utilizing solids is to carry out classification.If minor diameter particle forms agglomerate each other, and when this agglomerate has major diameter particle equal above sinking speed, then this agglomerate is recovered together with major diameter particle, and therefore effectiveness of classification is deteriorated.Therefore, preferably fragmentation carried out to the agglomerate of minor diameter particle and become single particle (primary particle).Importing room 12 by forming slip as in the present embodiment, fragmentation can be carried out to the offspring of minor diameter particle.And then when slip S imports the upper end of room 12 by slip and flows into the first recovery room, minor diameter particle becomes primary particle.
In order to carry out fragmentation more reliably, the mode preferably expanded along with the upper direction in (A) of trend Fig. 1 with the sectional area making slip import the cross section (cross section of the paper vertical direction in (A) of Fig. 1) of room 12 configures slip introduction part 15.When the inflow of slip S is positioned at above-mentioned scope, the ratio (S1/S2) of the sectional area S1 of position that the area of preferred above-mentioned cross section is maximum and the sectional area S2 of minimum position is 2.5 ~ 5.0, is more preferably 3.0 ~ 4.0.Such as, the slip introduction part 15 on the right side in (B) of Fig. 1 can be made from plumbness towards right to tilt 2 ~ 8 ° (being preferably 2 ~ 4 °), by making the slip introduction part 15 of above-below direction side erect setting in the mode do not tilted, the sectional area of cross section can be expanded.When above-mentioned inclination is lower than 2 °, cannot broken offspring fully.When above-mentioned be tilted beyond 8 ° time, the stream of slip is peeled off by from slip introduction part 15, and therefore the stream of slip becomes unstable.In the present embodiment, above-mentioned inclination is set as 4 °.Thus, the effectiveness of classification κ (D75/D25) reclaiming first the major diameter particle that room is recovered is 1.20 ~ 1.75.In addition, effectiveness of classification κ (D75/D25) refers to that the bottom 1/4 relative to upper 1/4 value (particle that particle diameter is greater than this particle diameter is the particle diameter of 25% of accumulative size-frequency curve) is worth the ratio of (same as described above, to be the particle diameter of 75%).
In addition, so-called " sectional area expands along with trend top " can be not only situation about expanding continuously along with trend top, also can be a part has same cross-sectional continuously shape along with trend top.Such as, can be formed as making sectional area expand continuously along with above trend from bottom, then there is along with trend top the shape of same cross-sectional continuously.
Further, in order to improve effectiveness of classification or make the higher limit of classification point increase, preferably near the upper end of slip importing room 12, acceleration mechanism is configured.Acceleration mechanism preferably can accelerate the speed of slip S while the stream not upsetting slip S.In the present embodiment, as shown in Figure 3, acceleration components 19 triangular in shape for longitudinal section is configured in slip in the mode that the sectional area of its cross section expands along with trend top to import near the upper end of room 12.In addition, make near the upper end of slip introduction part 15 vertical.At the sloping portion 15a by slip introduction part 15 along with above trend after expanding the sectional area of cross section, by the acceleration mechanism be made up of the vertical component 15b of acceleration components 19 and slip introduction part 15, the sectional area of cross section is reduced gradually along with trend upper end.By acceleration mechanism, accelerated by the flow velocity of slip S during slip importing 12 upper end, room, therefore the rectilinear propagation of minor diameter particle improves.Therefore, minor diameter particle is easy to move to the second recovery room.When minor diameter particle does not move to the second recovery room and is stranded in the first recovery room for a long time, there is minor diameter particle coacervation and form offspring and reclaim the misgivings of room sedimentation first.By accelerating the flow velocity of slip S, the cohesion of minor diameter particle can be prevented, effectiveness of classification κ can be improved.For acceleration mechanism, the flow velocity of slip S can be accelerated by the parts of other shapes of configuration, also can be formed slip by the mode narrowed near upper end with the sectional area making slip import room 12 and import the sidewall of room 12 and accelerate the flow velocity of slip S.
Further, when the flow velocity of slip S is fast, the major diameter particle of sinking speed block is easily made to move to the second recovery room.As mentioned above, by the flow velocity utilizing acceleration mechanism to accelerate slip S, the higher limit of classification point can be improved.
In addition, so-called classification point refers to: the distribution of the size distribution (measuring relative to the pen amount (Pen of particle diameter) of minor diameter particle in a fractionated and major diameter particle) in, the particle diameter identical in quality of major diameter particle and minor diameter particle.
The speed preferably utilizing above-mentioned acceleration mechanism to make slip be imported the upper end of room 12 by slip is 1.0 ~ 5.0m/s.When this speed is lower than 1.0m/s, the effect of acceleration mechanism cannot be obtained.When this speed is more than 5.0m/s, can upset the stream of the slip of the first recovery indoor, effectiveness of classification reduces.Further, due to the rate of climb of the slip of slurry level hope place in the first recovery room can be improved, therefore, it is possible to obtain fully for making minor diameter particle reclaim the propulsive force of room movement towards second.As a result, the higher limit of classification point can be made to increase.By selecting the speed of slip from above-mentioned scope, classification point can be adjusted, and can high-precision classification be carried out.
Further, the height h3 of deceleration component 19 is preferably 0.2 ~ 1.0 relative to the ratio (h3/h1) of the height h1 of slip importing room 12.When lower than 0.2 time, the acceleration distance of slip is not enough, and slip S therefore cannot be made to accelerate fully.Therefore, the higher limit of classification point diminishes, and the adjusting range of classification point narrows.When more than 1.0, the wall surface resistance that the boundary between acceleration mechanism and slip S produces becomes greatly, and therefore the acceleration of particle is hindered.
Weak in the adhesion of offspring, can easily broken, the sectional area that slip also can be made to import room 12 expands gradually along with trend top.Even if in this case, also room 12 can be imported at slip as required configure above-mentioned acceleration mechanism.
Import the slip S behind room 12 by slip and flow into the first recovery room 13.When first reclaim room be full of slip S time, the fast major diameter particle of sinking speed sinks down into the bottom of the first recovery room.On the other hand, the minor diameter particle that sinking speed is slow is trapped near the liquid level of slip S.
When the first amount reclaiming the slip S of room constantly increases, liquid level crosses the upper end of above-mentioned classification parts 16, slip S flows into second by the gap formed by the upper end of these classification parts 16 and the top of framework 11 and reclaims room 14.Thus, reclaim room 14 at the first minor diameter particle reclaimed near the liquid level being trapped in slip S in room 13 towards second to move.
Then, above-mentioned major diameter particle dump valve and above-mentioned minor diameter particle dump valve is opened, the slip utilizing grading plant to reclaim respectively to be dispersed with major diameter particle and be dispersed with the slip of minor diameter particle.Now, to make the discharge rate (flow of slip) from major diameter particle outlet 13a and minor diameter particle outlet 14a become the adjustment that suitable mode carries out flow.Such as, when too much from the discharge rate of major diameter particle outlet 13a, slip S does not reclaim room towards second and moves.On the contrary, when very few, the mobile quantitative change towards the second recovery room is many, result, and particle diameter is greater than the particle reclaiming the target grain size that room is reclaimed second and moves towards the second recovery room.
Near the bottom of the first recovery room 13 and the second recovery room 14, along with trend major diameter particle outlet 13a and minor diameter particle outlet 14a, the sectional area of cross section reduces respectively.Therefore, major diameter particle and minor diameter particle can not be deposited in the bottom of the first recovery room 13 and the second recovery room 14, but are discharged by from framework 11 efficiently.
When the area that first reclaims the cross section of room 13 is crossed wide, minor diameter particle implemented 13 sedimentations before room 14 is reclaimed in arrival second after first, and when narrow, major diameter particle collided with above-mentioned classification parts 16 before sedimentation.Therefore, the first sectional area S3 reclaiming the cross section of room at the top place of preferred above-mentioned slip importing room 12 selects from 2 ~ 10 relative to the ratio (S3/S2) of the sectional area S2 of the cross section of above-mentioned slip importing room 12.
Grading plant of the present invention can easily change classification point by the interval of changing between above-mentioned classification parts 16 and above-mentioned top board.In the present embodiment, by the structure that is formed as loading and unloading by classification parts 16 and the different classification parts 16 of the height (above-below direction in (A) of Fig. 1) that changes the outfit, can easily make classification o'clock at the scope change of 100 ~ 1000 μm.When the top that slip imports room 12 is too small with the difference of the height and position of the top of classification parts 16, major diameter particle is also admitted to the second recovery room 14, and when above-mentioned difference is excessive, the height of framework 11 becomes too high.Therefore, the height h2 of preferred above-mentioned classification parts 16 is 1.2 ~ 5.0 relative to the ratio (h2/h1) of the height h1 of slip importing room 12, is more preferably 1.2 ~ 3.0.
Grading plant of the present invention is separated into the first recovery room 13 and second by classification parts 16 and reclaims room 14, and, as long as there is slip can reclaim the space of room 13 towards the second recovery room 14 movement from first, be not limited to above-mentioned structure.Such as, the classification parts 16 possessing the opening portion that can block respectively can also be configured.By selecting the above-mentioned opening portion opened wide, classification point can be changed.Based on the reason identical with epimere, preferably to open wide opening portion bottom height relative to slip import room height ratio 1.2 ~ 5.0 scope.
Further, adjusting the boot speed guiding mechanism 18 of slip S towards the boot speed of framework 11 by being configured between slip introducing port 12a and the pump P1 as hoisting mechanism, classification point can be adjusted further.Pipe H3, H4 that the above-mentioned boot speed guiding mechanism 18 of present embodiment comprises valve V1 and links with this valve V1.Make above-mentioned pipe H1 branch, link at branch point connecting piece H3, pipe H4 and slurry vessel 22.Make the path branches between slip introducing port 12a and pump P1, make one side and slip introducing port 12a link and the opposing party and valve V1 are linked.Make it unlimited, a part of returns stock tank 22 of the ormal weight of slip S by the aperture of regulating valve V1.Therefore, it is possible to adjustment slip S is towards the boot speed of framework 11.
By reducing the rate of climb of the slip near the slurry level in the first recovery room, the lower limit of classification point can be reduced.But, when the reduction degree of the rate of climb exceed need time, cannot obtain for making minor diameter particle reclaim enough propulsive forces of room movement towards second.Therefore, in the present embodiment, the rate of climb of above-mentioned slip is selected from the scope of 0.003 ~ 0.050m/s.Further, as mentioned above, acceleration mechanism is utilized to make the speed being imported the slip of the upper end of room by slip be 1.0 ~ 5.0m/s.Thereby, it is possible to select classification point from the scope of 50 ~ 300 μm.
(blasting apparatus)
Secondly, the situation of blasting apparatus grading plant of the present invention being applied to wet type is described.Fig. 4 illustrates the structure of the blasting apparatus 20 of wet type of the present invention.Blasting apparatus 20 comprises shot-peening Processing Room 21, is configured in the slurry vessel 22 of the below of this shot-peening Processing Room and the particle in the slip S in slurry vessel 22 carried out to the sorting mechanism of classification.Further, the nozzle 23 for spraying slip S is configured with in the inside of shot-peening Processing Room 21.
Abrasive particle (grinding-material) dispersion (being water in the present embodiment) and the slip S that obtains in a liquid being used in and carrying out shot-peening processing is had at slurry vessel 22.Above-mentioned abrasive particle can be dry type, wet type, can be the various particles that usually can use in shot-peening processing as the particle of iron and non-ion made of iron (steel ball, abrasive material, guiding principle silk cutting pill) ceramic-like particle, plant particle, resinae particle and so on, there is no particular determination.Above-mentioned abrasive particle mixes in the mode of 5 ~ 60 volume % accounting for slip entirety, is dispersed in water.
In order to the bottom preventing abrasive particle to be settled down to slurry vessel 22, as mentioned above, be preferably configured with at above-mentioned slurry vessel 22 rabbling mechanism (not shown) making it disperse for stirring abrasive particle.
Slip S in this slurry vessel 22 is drawn by hoisting mechanism P2 (being shielding electrodynamic pump in the present embodiment) and is carried towards the nozzle 23 be configured in shot-peening Processing Room 21.The slip S being transported to nozzle 23 mixes with the gases at high pressure sent into from gases at high pressure occurring source 24 (being compressed air in the present embodiment), sprays towards machined object W as solid and gas liquid three-phase fluid.The slip sprayed flows into above-mentioned slurry vessel 22.Now, create slight crack by colliding with machined object W, the abrasive particle of breach, the cutting particle etc. of being processed the machined object W produced by shot-peening also flow into slurry vessel 22.In common shot-peening processing, abrasive particle can be made to circulate and repeatedly use, but create in the abrasive particle of slight crack, breach above-mentioned, there is the abrasive particle becoming the diameter being not suitable for shot-peening processing.That is, comprise the abrasive particle of diameter (cannot reuse) and the cutting particle etc. of machined object W that become and be not suitable for shot-peening processing in the slip S in slurry vessel 22, therefore need them to remove.Therefore, while carrying out shot-peening processing in the above described manner, above-mentioned sorting mechanism is utilized to carry out sorting.The abrasive particle returns stock tank 22 that can reuse utilizing above-mentioned sorting mechanism to sub-elect, and sprayed by nozzle 23 at this.
Above-mentioned sorting mechanism suitably can use grading plant 10 of the present invention.That is, can using the abrasive particle that can reuse in slip S as major diameter particle, using becoming the abrasive particle of the size that cannot reuse, the cutting particle etc. of machined object is separated respectively as minor diameter particle.The sauce being dispersed with the abrasive particle that can reuse is discharged and returns stock tank 22 from major diameter particle outlet 13a.On the other hand, be dispersed with become the size that cannot reuse abrasive particle, machined object the slip of cutting particle etc. be discharged from minor diameter particle outlet 14a.
The slip be discharged from minor diameter particle outlet 14a is carried by towards separating mechanism 25, carries out Separation of Solid and Liquid.Separation of Solid and Liquid can use the known methods such as continuous sedimentation thickener, filter press, centrifugal separating device, sieve, magnetic force sorting device.Such as, under abrasive particle the situation of the burr as forging (cold forging, forge hot) such as abrasive particle removing chrome-molybdenum steel such as the iron abrasive materials of use and the magnetic situation of the equal tool of machined object, preferably magnetic grader is used.
The isolated solids of separating mechanism 25 are utilized to reclaim as deposit.Isolated solid is recovered to deposit groove 26 as deposit.Isolated liquid storage is in hopper 27.This liquid can supplementing towards slurry vessel 22 along with the carrying out of shot-peening processing during the abrasive particle of decrement for adjusting the concentration of slip.Or, also may be used for the machined object W after cleaning shot-peening completion of processing.By utilizing hoisting mechanism P3 that this liquid is sent into cleaning nozzle 28, and spraying towards machined object together with the gases at high pressure sent into from gases at high pressure occurring source 24, the abrasive particle on the surface remaining in machined object W can be removed and cut particle.
Hoisting mechanism P1 and hoisting mechanism P2 can be made to be same hoisting mechanism.Such as, as shown in Figure 5, when only using hoisting mechanism P1, Shi Guan H1 branch, and this branch point can be linked to nozzle 23 via pipe.Now, also the emitted dose guiding mechanism 29 of adjustment slip S towards the import volume of nozzle 23 can be configured for from this branch point to the path of nozzle 23.Such as, this emitted dose guiding mechanism 29 can be used in one end and be linked with valve V2 and the other end is configured in body near slurry vessel 22.When opening this valve V2, slip S returns stock tank 22, therefore, it is possible to adjust the boot speed of slip S towards nozzle 23 by the aperture adjusting this valve.
Further, as mentioned above, also the boot speed guiding mechanism 18 ((A) with reference to Fig. 1) of adjustment slip S towards the boot speed of grading plant 10 can be configured at pipe H1.
When adjusting the boot speed of slip S towards grading plant 10 and the import volume towards nozzle 23, when needing to carry out finely tuning as valve, also can replace valve and use diameter to be less than the body (throttle pipe) of above-mentioned tubular body.Because the internal structure of valve is complicated, therefore when using the situation of the large slip S of wearing and tearing to there are the misgivings broken down.The failure ratio valve of throttle pipe is few, even if the increased wear of inside and be difficult to the adjustment of the boot speed carrying out slip S when, due to more cheap than valve, therefore, it is possible to easily change.
Although and not shown, in order to make shot-peening working ability stablize, also can be configured for the densimeter of concentration measuring slip.Can automatically or manually drop into abrasive particle or liquid towards slurry vessel according to the measurement result of densimeter thus make the constant concentration of slip.
As the first embodiment, illustrate and utilize grading plant of the present invention to carry out the result of classification to the slip mixing iron abrasive material (GH-3: average grain diameter 300 μm) and white fused alumina (WA#320: average grain diameter 40 μm).For slip, be respectively 40 volume % with the containing ratio of solids (abrasive particle), the mode of 10 volume % is scattered in water and is made into slip, the mode being 2.5m/s with the flow velocity of the slip making slip introducing port place imports the grading plant of present embodiment and carries out classification.Make the slip of discharging from major diameter particle outlet and minor diameter particle outlet be the sieve of 125 μm respectively by mesh opening, confirm to determine whether to be classified into major diameter particle and minor diameter particle by the color of the slip after this sieve by visualization.
Utilize sieve to carry out classification to the slip of discharging from major diameter particle outlet, results verification has a large amount of iron abrasive materials on sieve.Further, although by the gonorrhoea slightly of the slip after this sieve, be similar to water white transparency, therefore known, only mix the minor diameter particle and white fused alumina that there are trace.Further, utilize sieve to carry out classification to the slip of discharging from minor diameter particle outlet, there is iron abrasive material in results verification on sieve.Further, be gonorrhoea shape by the slip after sieve, therefore knownly mix, be dispersed with a large amount of white fused aluminas.According to above result, the grading plant of present embodiment can be utilized to carry out classification accurately.
Secondly, as the second embodiment, the example of situation about being used as the sorting unit of blasting apparatus by the grading plant of present embodiment is described.Iron abrasive material (GH-3: average grain diameter 300 μm) is made to be scattered in the slip of water in the mode that concentration is 30 quality % as slip.The nozzle of aspiration-type is utilized to be sprayed towards chromium steel steel (SCr) by this slip and carry out shot-peening processing.Nozzle is 100mm to the distance of machined object, and the pressure of hoisting mechanism P1 is 0.33MPa, and the pressure of gases at high pressure (compressed air) is 0.4MPa.
Make the angle of inclination of slip introduction part 15, the ratio (h3/h1) of height that the height of acceleration components 19 imports room relative to slip changes by the mode of table 1 respectively, and carry out shot-peening processing.After the injection through the moment of 30 minutes, reclaim slip respectively from major diameter particle outlet 13a and minor diameter particle outlet 14a.At 90 DEG C, drying is carried out to reclaimed slip, then utilize laser diffraction formula particle size distribution device (SALD-2100: Shimadzu Seisakusho Ltd.'s (strain) makes) to measure size distribution.The effectiveness of classification κ (D75/D25) of classification point and major diameter particle is calculated based on be measured to size distribution.
Table 1
Imported the ratio (h3/h1) of the height of room by the height at the angle of inclination and acceleration components 19 of changing slip introduction part 15 relative to slip, classification point can be changed.Usually, if effectiveness of classification κ is more than 1.0, classification can be carried out well, if more than 1.5, classification can be carried out admirably.The effectiveness of classification of embodiment 1 ~ 13, all more than 1.2, presents good result.Further, when the sorting unit using grading plant as blasting apparatus, so that minor diameter particle (becoming the cutting particle etc. of the abrasive particle of the size that cannot reuse, machined object) is removed as object from slip.Therefore, when classification point is set as about 90 μm, as described in Example 5, effectiveness of classification κ is 1.60.This illustrates that grading plant of the present invention can use well as the device of doing all one can of blasting apparatus.
The main label used below is shown in this description and accompanying drawing.
10: grading plant; 11: framework; 12: slip imports room; 12a: slip introducing port; Reclaim room at 13: the first; 13a: major diameter particle outlet; Reclaim room at 14: the second; 14a: minor diameter particle outlet; 15: slip introduction part; 16: classification parts; 17: slip introducing mechanism; 18: boot speed guiding mechanism; 19: acceleration components; 20: blasting apparatus; 21: shot-peening Processing Room; 22: slurry vessel; 23: nozzle; 24: gases at high pressure occurring source; 25: separating mechanism; 26: deposit groove; 27: hopper; 28: cleaning nozzle; 29: emitted dose guiding mechanism; P1, P2, P3: hoisting mechanism; W: machined object; S: slip; V1, V2: valve.
[utilizing possibility in industry]
Describe the example in the grading plant of the abrasive particle that the present invention to be applied in and can to reuse for sorting from the slip in the blasting apparatus of wet type and particle in addition in embodiments, but grading plant of the present invention can be applied to the purposes of all wet classifications such as foreign matter removing, ore dressing, sorting, fluid purification etc. in slip.
Claims (20)
1. a grading plant, this grading plant is for utilizing the difference of sinking speed to carry out the device of classification to the solids be dispersed in slip,
The feature of described grading plant is,
Described grading plant possesses:
Framework, imports this framework by described slip, and this framework is used for described slip to be classified into major diameter particle and minor diameter particle; And
Slip introducing mechanism, this slip introducing mechanism is used for slip to import described framework,
For described framework, be separated into the first recovery room and second by the classification parts of tabular in this framework and reclaim room, described classification parts erect from the bottom surface of described framework and arrange and have the upper end being provided with gap between the end face of described framework,
Reclaim indoor described first and be formed with slip importing room, the wall of slip introduction part or described slip introduction part and described first recovery room that the sidewall that this slip imports room erects the tabular of setting by the bottom surface of reclaiming room from described first is formed, the lower end importing room at described slip is formed with the slip introducing port linked with described slip introducing mechanism, further, described slip imports the open upper end of room.
2. a grading plant, this grading plant is for utilizing the difference of sinking speed to carry out the device of classification to the solids be dispersed in slip,
The feature of described grading plant is,
Described grading plant possesses:
Framework, imports this framework by described slip, and this framework is used for described slip to be classified into major diameter particle and minor diameter particle; And
Slip introducing mechanism, this slip introducing mechanism is used for slip to import described framework,
For described framework, be separated into the first recovery room and second by the classification parts of tabular in this framework and reclaim room, described classification parts erect from the bottom surface of described framework and arrange and have multiple opening portion that can block,
Reclaim indoor described first and be formed with slip importing room, the wall of slip introduction part or described slip introduction part and described first recovery room that the sidewall that this slip imports room erects the tabular of setting by the bottom surface of reclaiming room from described first is formed, the lower end importing room at described slip is formed with the slip introducing port linked with described slip introducing mechanism, further, described slip imports the open upper end of room.
3. grading plant according to claim 1 and 2, is characterized in that,
Can loading and unloading at least partially of described classification parts.
4. grading plant according to claim 1 and 2, is characterized in that,
Described slip imports room and is formed as the sectional area expansion along with trend top.
5. grading plant according to claim 1 and 2, is characterized in that,
The acceleration mechanism for accelerating slip is possessed in the upper end of described slip importing room.
6. grading plant according to claim 4, is characterized in that,
The acceleration mechanism for accelerating slip is possessed in the upper end of described slip importing room.
7. grading plant according to claim 5, is characterized in that,
Utilize described acceleration mechanism that the sectional area of described slip introduction part is reduced gradually along with trend top.
8. grading plant according to claim 6, is characterized in that,
Utilize described acceleration mechanism that the sectional area of described slip introduction part is reduced gradually along with trend top.
9. grading plant according to claim 1 and 2, is characterized in that,
Described slip introducing mechanism possesses the hoisting mechanism for promoting slip,
The boot speed guiding mechanism of the boot speed for adjusting described slip is configured with between described slip introducing port and described hoisting mechanism.
10. a blasting apparatus, this blasting apparatus is for being sprayed towards machined object with the blasting apparatus carrying out shot-peening processing together with gases at high pressure by the slip being dispersed with abrasive particle in a liquid,
The feature of described blasting apparatus is,
Described blasting apparatus possesses:
Shot-peening Processing Room, is configured with nozzle in the inside of this shot-peening Processing Room;
Slurry vessel, this slurry vessel is for storing described slip;
Sorting mechanism, this sorting mechanism is used for carrying out classification to the particle in the slip in described slurry vessel; And
Separating mechanism, this separating mechanism is used for carrying out Separation of Solid and Liquid to the slip comprising the minor diameter particle after by described grading plant classification,
Described sorting mechanism is the grading plant described in claim 1 or 2.
11. blasting apparatus according to claim 10, is characterized in that,
Described separating mechanism is magnetic force sorting device.
12. blasting apparatus according to claim 10, is characterized in that,
The cleaning nozzle for cleaning the machined object after shot-peening processing is configured with in described shot-peening Processing Room,
Described cleaning nozzle sprays the liquid gone out by described its disengagement.
13. 1 kinds of stage divisions, is characterized in that,
This stage division is the stage division using the grading plant described in claim 1 or 2 solids be dispersed in slip to be carried out to classification,
This stage division comprises:
Described slip is imported described slip from described slip introducing port and imports indoor operation;
The opening portion making be imported into described slip import the upper end of room from described slip is spread and the operation of discharging;
Make the minor diameter particle in the solids in described slip reclaim indoor moving by the gap between described classification parts and described end face or the opening portion being arranged at described classification parts towards described second, and make the major diameter particle precipitation in the solids in described slip reclaim the operation of the bottom of room to described first; And
Make the described minor diameter particle precipitation after moving to described second recovery indoor to the operation of the bottom of this second recovery room.
14. stage divisions according to claim 13, is characterized in that,
The diameter of the solids reclaiming room movement towards described second is changed by the distance changed between the lower end of distance between the upper end of described classification parts and described end face or described opening portion and described end face.
15. 1 kinds of stage divisions, is characterized in that,
This stage division is the stage division using the grading plant described in claim 5 solids be dispersed in slip to be carried out to classification,
This stage division comprises:
Described slip is imported described slip from described slip introducing port and imports indoor operation;
Utilize described acceleration mechanism to accelerate the described slip be imported into, and the opening portion making described slip import the upper end of room from described slip is spread and the operation of discharging;
Make the minor diameter particle in the solids in described slip reclaim indoor moving by the gap between described classification parts and described end face or the opening portion being arranged at described classification parts towards described second, and make the major diameter particle precipitation in the solids in described slip reclaim the operation of the bottom of room to described first; And
Make the described minor diameter particle precipitation after moving to described second recovery indoor to the operation of the bottom of this second recovery room.
16. 1 kinds of stage divisions, is characterized in that,
This stage division is the stage division using the grading plant described in claim 6 solids be dispersed in slip to be carried out to classification,
This stage division comprises:
Described slip is imported described slip from described slip introducing port and imports indoor operation;
Utilize described acceleration mechanism to accelerate the described slip be imported into, and the opening portion making described slip import the upper end of room from described slip is spread and the operation of discharging;
Make the minor diameter particle in the solids in described slip reclaim indoor moving by the gap between described classification parts and described end face or the opening portion being arranged at described classification parts towards described second, and make the major diameter particle precipitation in the solids in described slip reclaim the operation of the bottom of room to described first; And
Make the described minor diameter particle precipitation after moving to described second recovery indoor to the operation of the bottom of this second recovery room.
17. 1 kinds of stage divisions, is characterized in that,
This stage division is the stage division using the grading plant described in claim 9 solids be dispersed in slip to be carried out to classification,
This stage division comprises:
Described slip is imported described slip from described slip introducing port and imports indoor operation;
The opening portion making be imported into described slip import the upper end of room from described slip is spread and the operation of discharging;
Make the minor diameter particle in the solids in described slip reclaim indoor moving by the gap between described classification parts and described end face or the opening portion being arranged at described classification parts towards described second, and make the major diameter particle precipitation in the solids in described slip reclaim the operation of the bottom of room to described first; And
Make the described minor diameter particle precipitation after moving to described second recovery indoor to the operation of the bottom of this second recovery room,
The diameter of the solids reclaiming room movement towards described second is changed by the boot speed of the slip changing described boot speed guiding mechanism place.
18. 1 kinds of method for blastings, is characterized in that,
This method for blasting is the method for blasting using the blasting apparatus described in claim 10 to carry out,
This method for blasting comprises:
In described slurry vessel, drop into liquid and abrasive particle and make it to disperse and obtain the operation of slip;
By the slurry pipeline transport in described slurry vessel to described nozzle, and mix with gases at high pressure and utilize the operation that described nozzle sprays towards machined object;
The cutting particle of sprayed slip and machined object is stored in the operation of slurry vessel;
By the slurry pipeline transport of described slurry vessel to the operation of described sorting mechanism;
The operation of slurry vessel is again delivered to as the solids being used for carrying out shot-peening processing using reclaiming in room described first the major diameter particle that is recovered to; And
Using the operation that the minor diameter particle be recovered in described second recovery room reclaims as deposit.
19. 1 kinds of method for blastings, is characterized in that,
This method for blasting is the method for blasting using the blasting apparatus described in claim 11 to carry out,
This method for blasting comprises:
In described slurry vessel, drop into liquid and the magnetic abrasive particle of tool and make it to disperse and obtain the operation of slip;
By the slurry pipeline transport in described slurry vessel to described nozzle, and mix with gases at high pressure and utilize the operation that described nozzle sprays towards the magnetic machined object of tool;
The cutting particle of sprayed slip and machined object is stored in the operation of slurry vessel;
By the slurry pipeline transport of described slurry vessel to the operation of described sorting mechanism;
The operation of slurry vessel is again delivered to as the solids being used for carrying out shot-peening processing using reclaiming in room described first the major diameter particle that is recovered to;
The operation of slurry pipeline transport to described magnetic force sorting device that described second reclaims the minor diameter particle that room is recovered to will be included in; And
Magnetic force is utilized to carry out the operation of Separation of Solid and Liquid to the slip being delivered to described magnetic force sorting device.
20. 1 kinds of grading plants, this grading plant is for utilizing the difference of sinking speed to carry out the grading plant of classification to the solids be dispersed in slip,
The feature of described grading plant is,
Described grading plant possesses:
The framework of tubular, imports this framework by described slip, and this framework is used for described slip to be classified into major diameter particle and minor diameter particle; And
Slip introducing mechanism, this slip introducing mechanism for importing described slip,
Described framework possesses: the classification parts of tabular, these classification parts erect setting from the bottom surface of described framework in the mode being provided with gap between the end face of described framework, and described framework are separated into the first recovery room being formed with major diameter particle outlet in bottom surface and the second recovery room being formed with minor diameter particle outlet in bottom surface; And
The slip introduction part of tabular, this slip introduction part configures upward from the described first bottom surface of reclaiming between the slip introducing port of the bottom surface opening of room and described major diameter particle outlet, spread upward for making to be fed to the described first slip reclaiming indoor from described slip introducing port
Described slip introducing mechanism one end is communicated with described slip introducing port, the other end is communicated with hoisting mechanism.
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2011123863 | 2011-06-02 | ||
| JP2011-123863 | 2011-06-02 | ||
| JP2012051173 | 2012-03-08 | ||
| JP2012-051173 | 2012-03-08 | ||
| PCT/JP2012/064113 WO2012165560A1 (en) | 2011-06-02 | 2012-05-31 | Classification device, and classification method, blast machining device provided with this classification device, and blast machining method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103338867A CN103338867A (en) | 2013-10-02 |
| CN103338867B true CN103338867B (en) | 2015-07-08 |
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| JP (1) | JP5915650B2 (en) |
| KR (1) | KR101933138B1 (en) |
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| JP6249929B2 (en) * | 2014-03-27 | 2017-12-20 | 株式会社神戸製鋼所 | Continuous surface treatment method for steel wire |
| CN105906088A (en) * | 2016-06-16 | 2016-08-31 | 赵登强 | High-efficiency and high-strength mineral water purifying device |
| CN105906090A (en) * | 2016-06-16 | 2016-08-31 | 赵登强 | Coal mine water recycling and purifying device |
| CN105906092A (en) * | 2016-06-16 | 2016-08-31 | 赵登强 | Coal mine water purifying device |
| CN105906089A (en) * | 2016-06-16 | 2016-08-31 | 赵登强 | High-efficiency mineral water purifying device |
| CN105906091A (en) * | 2016-06-16 | 2016-08-31 | 赵登强 | High-durability purification device for coal mine water |
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- 2012-05-31 KR KR1020137020155A patent/KR101933138B1/en active IP Right Grant
- 2012-05-31 CN CN201280007188.1A patent/CN103338867B/en active Active
- 2012-05-31 JP JP2013518167A patent/JP5915650B2/en active Active
- 2012-05-31 WO PCT/JP2012/064113 patent/WO2012165560A1/en active Application Filing
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| DE4026063A1 (en) * | 1990-03-27 | 1992-02-20 | Lindemann Maschfab Gmbh | Vibratory fluidised bed for sorting scrap metal - uses multi-layer bed to avoid need for air blast at outlet end of bed |
| JPH08141913A (en) * | 1994-11-10 | 1996-06-04 | Alps Eng:Kk | Blast machining device |
| JPH10166272A (en) * | 1996-12-12 | 1998-06-23 | Tokyo Giken:Kk | Wet blast device and polishing work method |
| JP2006175526A (en) * | 2004-12-20 | 2006-07-06 | Dainippon Printing Co Ltd | Blast method and device |
| CN102026699A (en) * | 2007-12-05 | 2011-04-20 | 康斯乔最高科学研究公司 | Micro-device and method for non-invasive and selective separation and extraction of particles in polydispersed suspensions, production method, and the applications thereof |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN103338867A (en) | 2013-10-02 |
| KR20140015318A (en) | 2014-02-06 |
| WO2012165560A1 (en) | 2012-12-06 |
| JPWO2012165560A1 (en) | 2015-02-23 |
| KR101933138B1 (en) | 2018-12-27 |
| JP5915650B2 (en) | 2016-05-11 |
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