CN106179785A - The fall cyclone bar shaped unit integrated technologies such as overflow fineness appreciation one one liter of nothing of fall - Google Patents
The fall cyclone bar shaped unit integrated technologies such as overflow fineness appreciation one one liter of nothing of fall Download PDFInfo
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- CN106179785A CN106179785A CN201610756169.9A CN201610756169A CN106179785A CN 106179785 A CN106179785 A CN 106179785A CN 201610756169 A CN201610756169 A CN 201610756169A CN 106179785 A CN106179785 A CN 106179785A
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- Prior art keywords
- overflow
- fall
- cyclone
- bar shaped
- cone
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/24—Multiple arrangement thereof
- B04C5/28—Multiple arrangement thereof for parallel flow
-
- 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
- B03B7/00—Combinations of wet processes or apparatus with other processes or apparatus, e.g. for dressing ores or garbage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/02—Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
- B04C5/04—Tangential inlets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
- B04C5/13—Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow
Abstract
The present invention relates to the fall cyclone bar shaped unit integrated technologies such as a kind of overflow fineness appreciation one one liter of nothing of fall, specifically existing two section of two closed circuit overflow fineness is appreciated " one high and one low "+wait fall cyclone+annular unit integrated technology, it transform the fall cyclone+bar shaped unit integrated technologies such as overflow fineness appreciation " fall one liter "+nothing as, solve primary grinding amount and secondary grinding amount balances；What the present invention was important implements the strong point is exactly that the fall cyclone such as Φ 660 and Φ 500mm background technology used is become Φ 660 and Φ 500mm to drop cyclone bar shaped set structure without waiting by original annular unit structure of modification.Specifically, first paragraph classifying equipoment Φ 660mm without etc. fall cyclone according to cyclone contour stealth be converted into inward eddy operation principle design separate cone long measure be that L=235mm accounts for the 17.66% of total long 1331mm of cylinder cone.Second segment classifying equipoment Φ 500mm bores a length of 184mm without waiting fall cyclone to separate, and compared with waiting fall cyclone 215mm, separates cone contraction in length 31mm.
Description
Technical field
The present invention relates to the fall cyclone bar shaped unit integrated technologies such as a kind of overflow fineness appreciation one one liter of nothing of fall, low in genus
Grade collophane and other mineral grind gradings be theoretical and technology.
Technical background
The fall cyclone annular units such as annular unit Φ 660mm are all used at the cyclone unit that grinding classification system is conventional
Pulp-inlet pipe 10 is arranged on unit bottom, and slurry is entered slurry dispenser 3 by Pulp pump pump pressure through pulp-inlet pipe 10, is assigned to 4 for 2
The fall cyclones 1 such as (4 operations 2 are standby) Φ 660mm, hydrocyclone sand is drained into sand setting case 7, through sand setting channel nozzle 11 row
Enter to sand setting sampling cabinet 12, return primary grinding machine through sand setting outlet and regrind.Overflow product enters overflow through outer overflow pipe 2
Case 6, then through spill box overflow discharge connection 14, enter overflow sampling cabinet 13, it is discharged to two-stage nitration through overflow sampling cabinet discharge pipe 16
After Product mix is arranged with two-stage nitration mill in ore mill ore discharge pump pond, squeeze into the fall cyclone annular units such as Φ 500mm with Pulp pump.
The fall cyclone annular unit such as Φ 500mm enters pipe 10 and is arranged on unit bottom, and slurry is pumped through entering by Pulp pump
Slurry pipe 10 enters slurry dispenser 6, is assigned to 6 for fall cyclones 3 such as 3 (6 operations 3 are standby) Φ 500mm, and cyclone sinks
Sand is drained into sand setting case 1, is drained into sand setting sampling groove 8 through sand setting channel nozzle, returns secondary grinding machine again through sand setting outlet
Mill.Overflow product enters spill box 4 through outer overflow pipe 2, then enters overflow sampling cabinet 9 through spill box overflow discharge connection,
Follow-up flotation operation agitator is entered through overflow sampling cabinet discharge pipe.
There are serious point of slurry inequality, No. 6 hydrocyclone sands in the fall cyclone annular unit such as background (existing) technology Φ 660mm
Drawing dry tie rod, No. 3 hydrocyclone sands to have loose bowels, the former overflow is run thick and the latter is then thin and dilute, and its result is as shown in table 1.Φ
The fall cyclone annular unit such as 500mm is also to there is a point slurry inequality, and its result is as shown in table 2.
Two grooves, in addition to point slurry granularity inequality, owing to sand setting and overflow stream are in changeless position, are not stopped by annular unit
Impact, single-point abrasion especially severe, cause whole casing short-term to have to because of single-point spillage a complete set of replacing, cause greatly
Waste.
Being open trough additionally, due to annular unit discharging opening, ore pulp fog is soaring, environmental pollution especially severe.For example
Such as alumina producer, grind grading runs under the conditions of high temperature 95 DEG C and high-alkali 200 gram liters, and uncovered two grooves cannot ensure safe life
Produce, personal safety accident can occur at any time.
Summary of the invention:
Too high and the closed circuit Φ of two-stage nitration for fall cyclone overflow fineness appreciations such as annular one section of closed circuit Φ 660mm of unit
The fall cyclone overflow fineness such as 500mm appreciates too low；The fall cyclone annular unit such as Φ 660mm enters slurry from unit bottom to be caused point
Slurry granularity is uneven, opens one sand setting of three cyclones and draws dry tie rod, and overflow is run slightly, a sand setting is had loose bowels, and overflow is the thinnest but also dilute
Deng three big problems.The present invention provides the fall cyclone bar shaped unit integrated technologies such as a kind of overflow fineness appreciation one one liter of nothing of fall.Tool
Body say be existing two section of two closed circuit overflow fineness is appreciated " one high and one low "+wait fall cyclone+annular unit integrated technology, transform
Fall cyclone+bar shaped unit the integrated technologies such as " fall one liter "+nothing of appreciating for overflow fineness, solve primary grinding amount and grind with two-stage nitration
Ore tonnage balance.
The fall cyclone bar shaped unit integrated technologies such as stream fineness of the present invention appreciation one one liter of nothing of fall are completed by having structure:
It is characterized in that slurry or slurry to be fractionated are respectively enterd every point of ore deposit again by after slurry pump pressure (11) press-in pulp-inlet pipe (15)
Pipe (6), slurry to be fractionated by every point pipe (6) distribute to by several Φ 660mm without etc. the bar shaped that cyclone (1) is constituted is dropped
The desilting product that falls cyclone (1) such as in unit, each charging aperture on cyclone top drops in nothing etc., each nothing obtain passes through sand-precipitating tube
(4) it is flowed into sand setting mixing machine (8), returns to one section of ball mill through desilting discharge pipe (14) and regrind；The fall cyclone such as each nothing
(1) the overflow product obtained enters U-shaped overflow launder (2) through overflow pipe (16), and U-shaped overflow launder (2) is discharged through overflow after collecting
House steward (13) collects in overflow mixer (10) again, it is simple to overflow intermediate products sample, and overflow intermediate products mix through overflow again
After material outlet enters two-stage nitration mill ore discharge Pulp pump pump pond mixes with Secondary grinding mill ore discharge, last overflow intermediate products pass through to have again
Pulp pump be pumped to by several Φ 500mm without etc. the fall cyclone top charging such as each nothing in the fall bar shaped unit that constitutes of cyclone
Mouth processes.
4 Φ 660mm of described first paragraph classifying equipoment without etc. fall cyclone form integrated bar shaped unit be by two row or
The three horizontally-arranged arrangement modes of row assemble；Described Φ 660mm without waiting fall cyclone bar shaped machine component to use 2 for 2 forms, then 2
The fall cyclone standby modes such as fall cyclone operation, other 2 Zhi Wu such as nothing.
6 Φ 500mm of described second segment classifying equipoment without etc. fall cyclone form integrated bar shaped unit be by two row or
The three horizontally-arranged arrangement modes of row assemble；Described Φ 500mm without waiting fall cyclone bar shaped unit to use 4 for 2 forms, then 4 nothings
Deng the fall cyclone standby modes such as fall cyclone operation, other 2 Zhi Wu, point slurry epigranular.
In described first paragraph classifying equipoment use Φ 660mm without wait fall cyclone be by stock inlet (5), outer overflow connection
Flange (2), enter slurry (7), cover plate (3), interior overflow (6), outer overflow pipe (1), pressure release pipe (15), cylinder cone (9), separate
Cone (11), sand setting nozzle (13) composition, its type of attachment is, stock inlet (5) is overall structure with entering slurry (7), cover plate (3) with enter
Slurry (7) uses cover plate adpting flange (4) to connect, interior overflow (6) uses tapering to insert outer overflow adpting flange with cover plate (3)
(2) compressing, outer overflow adpting flange (2) is connected, outer overflow pipe (1) is connected by each other with cover plate (3) employing in outer overflow (1)
Outer overflow anchor ear (14) connects, and pressure release pipe (15) and outer overflow pipe (1) are overall structure, cylinder cone (9) with enter slurry (7)
Using cylinder cone adpting flange (8) to connect, separation cone (11) separates cone anchor ear (10) with cylinder cone (9) employing and connects, desilting tip
(13) with separate cone (11) use desilting tip anchor ear (12) connect, pressure release pipe (15) be arranged on outer overflow pipe (1) sidepiece and
Communicate with outer overflow pipe (1).
In described second segment classifying equipoment use Φ 500mm without wait drop cyclone be by stock inlet (5), enter slurry (7),
Cover plate (3), interior overflow (6), outer overflow pipe (1), pressure release pipe (15), cylinder cone (9), separation cone (11), sand setting nozzle (13)
Composition.Its type of attachment is, stock inlet (5) with enter slurry (7) be overall structure, cover plate 3 and enter slurry (7) use cover plate be connected
Flange (4) connects, interior overflow (6) uses tapering to insert outer overflow adpting flange (2) compression, outer overflow (1) and lid with cover plate (3)
Plate (3) uses outer overflow adpting flange (2) to connect, and outer overflow pipe (1) is connected by outer overflow anchor ear (14) each other and connects, presses
Power release pipe (15) and outer overflow pipe (1) are overall structure, and cylinder cone (9) uses cylinder cone adpting flange (8) with entering slurry (7)
Connect, separate cone (11) and cylinder cone (9) use separates cone anchor ear (10) connect, desilting tip (13) and separate cone (11) employing and sink
Husky nozzle anchor ear (12) connects, and pressure release pipe (15) is arranged on outer overflow pipe (1) sidepiece.And communicate with outer overflow pipe (1).
Described first paragraph classifying equipoment Φ 660mm without etc. fall cyclone according to cyclone contour stealth be converted into inward eddy work
Separation cone long measure L=215mm of principle design～235mm, account for the 17.66% of total long 1331mm of cylinder cone.
Described second segment classifying equipoment Φ 500mm without etc. fall cyclone be based on cyclone contour stealth and be converted into inward eddy work
Making principle design, it separates cone long measure L=188～200mm, accounts for the 18.46% of total cylinder cone length 1083mm.
First paragraph Φ 660mm of the present invention and two-stage nitration Φ 500mm without etc. fall cyclone bar shaped set structure form feature, from machine
Group top is entered slurry, is increased single cyclone treating capacity, reduces cyclone and use number, reduce into slurry pressure, arrange sand sediment pipe, U
The big technological innovation of type overflow launder four, solve cyclone divide slurry granularity be uneven, sand setting draws dry tie rod, have loose bowels, overflow run thick, overflow
Flow the thinnest but also dilute work abnormal.Sand sediment pipe, U-shaped overflow launder extend service life, and safety and environmental protection produces, and maintenance management is convenient
Plurality of advantages.
Fall cyclone+bar shaped unit the integrated technologies such as one overflow fineness of the present invention appreciation " fall one liter "+nothing, it can carry
High grinding efficiency and classification efficiency.The appreciation of first paragraph overflow fineness is from 60.94-29.64=31.30 percentage of background technology
Point, is reduced to the technology of the present invention 43-20=23 percentage point.The appreciation of second segment overflow fineness is from the 90.00-of background technology
49.93=40.07 percentage point, bring up to 86.00-36=50 percentage point of inventive technique.One section of overflow fineness appreciates and drops
Low 8.3 percentage points, two-stage nitration overflow fineness appreciates and improves 9.93 percentage points.Background technology ore grinding amount 183t/h raw ore,
Power consumption 25.87kW h/t raw ore.The technology of the present invention ore grinding amount 220t/h raw ore, power consumption 21.95kW h/t raw ore.Two-stage nitration classification
Efficiency background technology 61.52%, the technology of the present invention 63.76%.
Accompanying drawing explanation
Fig. 1 Φ of the present invention 660 without etc. fall cyclone structural representation.
Fig. 2 Φ of the present invention 500 without etc. fall cyclone structural representation.
The structural representation of cyclone such as fall such as Φ 660 grade in Fig. 3 prior art.
The structural representation of cyclone such as fall such as Φ 500 grade in Fig. 4 prior art.
The annular unit structural representation being made up of fall cyclones such as six Φ 660 in Fig. 5 prior art.
Fig. 6 is the vertical view direction structure signal being circularized unit in Fig. 5 prior art by fall a cluster cyclones such as six Φ 660
Figure.
The annular unit structural representation being made up of fall cyclones such as 9 Φ 500 in Fig. 7 prior art.
Fig. 8 is the vertical view direction structure signal being circularized unit in Fig. 7 prior art by fall a cluster cyclones such as 9 Φ 500
Figure.
Fig. 9 present invention by 4 Φ 660 without etc. the fall above row that forms of cyclone and a following row constitute two rows
Bar shaped set structure schematic diagram.
Figure 10 is that Fig. 9 present invention is in strip the vertical view direction structure schematic diagram of unit by fall a cluster cyclones such as 4 Φ 660.
Figure 11 is that Fig. 9 present invention is in strip the side-looking direction structure schematic diagram of unit by fall a cluster cyclones such as 4 Φ 660.
Figure 12 present invention by 6 Φ 500 without etc. the structure of upper, middle and lower three row arrangement bar shaped unit that forms of fall cyclone
Schematic diagram.
Figure 13 is that Figure 12 present invention is in strip the vertical view direction structure schematic diagram of unit by fall a cluster cyclones such as 4 Φ 500.
Figure 14 is that Figure 12 present invention is in strip the side-looking direction structure schematic diagram of unit by fall a cluster cyclones such as 4 Φ 500.
Figure 15 Φ of the present invention 660 etc. fall a cluster cyclone be in strip unit and Φ 500 etc. fall a cluster cyclone be in strip unit with
Miscellaneous equipment installs the annexation of relation (in production process route).
Each label in figure:
1 outer overflow pipe；2 outer overflow adpting flanges；3 cover plates；4 cover plate adpting flanges；5 stock inlets；In 6
Overflow；7 enter slurry；8 cone adpting flanges；9 cones；10 separate cone anchor ear；11 separate cone；13 sand settings
Nozzle；14 separate cone anchor ear；15 pressure release pipes.
21 raw ore belts are to ore deposit；22 Φ 660 without etc. fall cyclone；23 first paragraph ball millings；24 Pulp pump；25—
Slime dam；26 Φ 500 without etc. fall cyclone；27 second segment ball millings；28-Pulp pump；29-slime dam；20-overflows to float
Choosing.
31 fall cyclones such as Φ 660 grade；32 outer overflow pipes；33 feed distributors；34 Pressure gauges；35—DN200
Pneumatic gate valve；36 spill boxes；37 sand setting casees；38 cyclone retainer ring；39 outer lower limbs；40 charging adapters；41 sink
Sandbox connecting tube；42 sand setting sampling cabinets；43 overflow sampling cabinets；44 overflow discharge connections；45 sand setting cover plates, 46 rotations
Stream device cover plate, 47 cyclone cover plate bracing frames, 48 cyclone adapters.
51 rifflers；52 overflow pipes；53 fall cyclones such as Φ 500 grade；54 overflow launders；55 pneumatic gate valves；
56 allotters；57 supports；58 sand setting sampling grooves；59 overflow sampling grooves；50 feed pipes.
The fall cyclones such as 61 nothings；62 U-shaped overflow pipes；63 supports；64 sand-precipitating tubes；65 sand settings collect cylinder；
66 points of pipes；67 adjust pipe (A)；68 sand setting mixing machines；69 overflow mixer outlets；70 overflow mixers；
71 slurry pump pressures；72 adjust pipe (B)；73 overflow discharge headers；74 sand setting discharge pipes；75 pulp-inlet pipes, 76 overflow
Flow tube, 77 pressure release pipes.
Detailed description of the invention
The mid-low grade collophanite ore Phosphate minerals proportion that the present invention processes without waiting fall cyclone bar shaped unit is between 2.8～3.2
Between, aluminosilicate gangue mineral proportion about 2.6, difference in specific gravity is between 0.2～0.6, by its etc. fall theory can be considered without etc.
Fall mineral, classification grade boundary line can divide according to the fineness of purpose Phosphate minerals liberation degree of minerals, it is not necessary to considers and gangue mineral
Difference in specific gravity.In other words, without etc. fall cyclone be with size divide classification boundary line reclaim target minreal, and wait drop cyclone be
To divide classification boundary line recovery target minreal than grade width great, that granularity is little and proportion is little, particle diameter is big.The former unit is grain
Footpath size, the latter's unit is grade width, and size is exactly a point, and grade width is exactly a line segment length, " point " with
There is the difference that character is different between the two in " line segment ", thus etc. fall cyclone for without etc. fall mineral in be do not meet objective
Rule.
What the present invention was important the implement fall cyclone such as Φ 660 and Φ 500mm that the strong point is exactly to be used background technology by
Annular unit structure of modification originally become Φ 660 and Φ 500mm without etc. fall cyclone bar shaped set structure.Specifically, first paragraph
Classifying equipoment Φ 660mm without etc. the fall cyclone separation cone that is converted into the design of inward eddy operation principle according to cyclone contour stealth long
Degree unit is that L=235mm accounts for the 17.66% of total long 1331mm of cylinder cone.Second segment classifying equipoment Φ 500mm is without waiting fall cyclone
Separate and bore a length of 184mm, compared with waiting fall cyclone 215mm, separate cone contraction in length 31mm.
The fall cyclone bar shaped unit integrated technologies such as two section of two closed circuit grinding classification system classification nothing of the present invention, first paragraph
It is connected with each other by conventional conveyance conduit, groove and sand pump between two closed circuit grindings and second segment two closed circuit grinding, it is characterised in that
Two-stage nitration two closed circuit grinding classification system uses the fall cyclone bar shaped units such as several nothings to carry out staged care, wherein first paragraph classification
Equipment uses several Φ 660mm without waiting fall cyclone to constitute an integrated bar shaped unit；Second segment classifying equipoment uses several
Φ 500mm without etc. fall cyclone constitute another integrated bar shaped unit；
First paragraph classifying equipoment is independently mounted in first paragraph two closed circuit grinding classification system；Second segment classifying equipoment is independent
It is arranged in second segment two closed circuit grinding classification system.
In first paragraph classifying equipoment use Φ 660mm without wait drop cyclone be by stock inlet 5, outer overflow adpting flange 2,
Enter slurry 7, cover plate 3, interior overflow 6, outer overflow pipe 1, pressure release pipe 15, cylinder cone 9, separate cone 11, sand setting nozzle 13 and form, its
Type of attachment is, stock inlet 5 with enter slurry 7 for overall structure, cover plate 3 with enter slurry 7 use cover plate adpting flange 4 to be connected, interior
Overflow 6 and cover plate 3 use tapering to insert outer overflow adpting flange 2 and compress, and outer overflow 1 uses outer overflow adpting flange 2 with cover plate 3
Connect, outer overflow pipe 1 is connected by outer overflow anchor ear 14 each other and connects, and pressure release pipe 15 and outer overflow pipe 1 are overall knot
Structure, cylinder cone 9 uses cylinder cone adpting flange 8 to be connected with entering slurry 7, separates cone 11 and separates cone anchor ear 10 with cylinder cone 9 employing
Connecting, desilting tip 13 connects with separating cone 11 employing desilting tip anchor ear 12, and pressure release pipe 15 is arranged on outer overflow pipe 1 sidepiece.
The Φ 500mm used in second segment classifying equipoment drops cyclone and is by stock inlet 5 without waiting, enters slurry 7, cover plate 3, interior
Overflow 6, outer overflow pipe 1, pressure release pipe 15, cylinder cone 9, separation cone 11, sand setting nozzle 13 form.Its type of attachment is, enters slurry
Mouthfuls 5 with to enter slurry 7 be overall structure, cover plate 3 and enter that slurry 7 uses cover plate adpting flange 4 to be connected, interior overflow 6 uses with cover plate 3
Outer overflow adpting flange 2 compresses, outer overflow 1 uses outer overflow adpting flange 2 to be connected with cover plate 3, outer overflow pipe 1 phase in tapering insertion
Be connected by between Hu that outer overflow anchor ear 14 connects, pressure release pipe 15 is overall structure with outer overflow pipe 1, cylinder cone 9 with enter slurry
Body 7 uses cylinder cone adpting flange 8 to connect, separate cone 11 use with cylinder cone 9 separate cone anchor ear 10 connect, desilting tip 13 with point
Connecting from cone 11 employing desilting tip anchor ear 12, pressure release pipe 15 is arranged on outer overflow pipe 1 sidepiece.
First paragraph classifying equipoment Φ 660mm without etc. fall cyclone be converted into inward eddy operation principle according to cyclone contour stealth
Separation cone long measure L=215mm of design～235mm, account for the 17.66% of total long 1331mm of cylinder cone.
Second segment classifying equipoment Φ 500mm without etc. fall cyclone be according to cyclone contour stealth be converted into inward eddy work former
Reason design, it separates cone long measure L=188～200mm, accounts for the 18.46% of total cylinder cone length 1083mm.
The present invention uses integrated bar shaped unit, then by fall eddy flows such as several (typically 4 6) nothings without waiting fall cyclone
Device is horizontally-arranged by two row or the horizontally-arranged arrangement of three row assembles, and in parallel construction, forms or gather one bar shaped unit of composition；After assembling
Bar shaped unit in the fall cyclone such as each nothing be the equipment that each works alone, each without etc. fall cyclone do not do
Disturb.During use, if collection is in strip unit and uses 2 for 2, then the running of the fall such as two nothings of manual control cyclone, two other nothing
Stand by Deng fall cyclone.
The present invention uses top to drop cyclone for slurry (charging) mode, the most each nothing etc. without waiting fall cyclone bar shaped unit
Stock inlet (charging aperture) is positioned at top, and discharging opening is in bottom.Collection be in strip unit feed pipe may first with large diameter pipe to bar
Shape unit top, then the fall cyclone apex such as nothing are entered by the minor diameter conveyance conduit of several band valves.
Slurry of the present invention has a slurry pump pressure 11 press-in pulp-inlet pipe 15 entrance point pipe 6 to distribute to 2 slurry to be fractionated for 2
Φ 660mm without waiting fall cyclone 1, cyclone desilting product is flowed into sand setting mixing machine 8 by sand-precipitating tube 4, discharges through desilting
Pipe 14 returns to one section of ball mill and regrinds.Overflow product enters through overflow pipe 16 and always discharges through overflow after U-shaped overflow launder 2 collects
Pipe 13 collects in overflow mixer 10 again, it is simple to overflow product samples, then enters two-stage nitration mill ore discharge through overflow batch mixing outlet
After Pulp pump pump pond mixes with Secondary grinding mill ore discharge, Pulp pump is had to be pumped to Φ 500mm without waiting fall cyclone bar shaped unit.
Slurry of the present invention is entered point pipe 6 by slurry pump pressure 11 press-in pulp-inlet pipes 15, is distributed to by slurry to be fractionated with 4 standby
2 Φ 500mm are without waiting fall cyclone 1, and cyclone desilting product imports desilting mixing machine 8, through desilting discharge pipe 14 by sand-precipitating tube 4
Return two-stage nitration ball milling ore mill to regrind.Overflow product enters after U-shaped overflow launder 2 collects through overflow drain through overflow pipe 16
13, again collect in overflow mixer 10, it is simple to overflow product samples, then enters succeeding level-two flotation through overflow batch mixing outlet
Operation agitator.
Φ 660mm of the present invention is without waiting fall cyclone bar shaped machine component slurry epigranular, and two Φ 660mm run are without waiting fall
Hydrocyclone sand concentration 77.53～78.93%, sand setting folder thin 7.14～8.30%-200 mesh, effluent concentration 46.12～
47.77%, overflow fineness 43.51～46.54%-200 mesh.
Φ 500mm of the present invention is without waiting fall cyclone bar shaped machine component slurry epigranular, and 4 Φ 500mm run are without waiting fall
Hydrocyclone sand concentration 71.22～72.54%, sand setting folder thin 16.38～17.01%-200 mesh, effluent concentration 27.56～
29.35%, overflow fineness 86.41～87.47%-200 mesh.
Φ 660mm of the present invention and Φ 500mm without etc. fall cyclone bar shaped unit in sand-precipitating tube 4, utilize sand setting rush sand setting make
By the protective action achieved at the bottom of sand setting flings tin, reach the purpose increased the service life.Sand-precipitating tube is added a cover and is realized safety and environmental protection
Produce.U-shaped overflow launder is added a cover and is realized safety and environmental protection production.Sand-precipitating tube and U-shaped overflow launder are easy to safeguard replacing.
The fall cyclone annular unit granularity such as table 1 Kunyang flotation mill background technology Φ 660mm divides slurry uneven result.
The fall uneven result of cyclone annular machine component slurry such as table 2 Kunyang flotation mill prior art Φ 500mm.
Table 3 Kunyang flotation mill the technology of the present invention Φ 660mm and Φ 500mm without etc. fall cyclone bar shaped machine component slurry grain
Degree uniform results.
Fall cyclone annular unit granularity such as table 1: Kunyang flotation mill background technology Φ 660mm etc. divides slurry uneven result
Note: 6# sand setting tie rod draws dry, 3# sand setting is had loose bowels whitewashing.
The fall uneven result of cyclone annular machine component slurry such as table 2: Kunyang flotation mill Φ 500mm etc.
Note: October 30 2015 Date of Sampling
Table 3: Kunyang flotation mill inventive technique Φ 660mm and Φ 500mm without etc. fall cyclone bar shaped machine component slurry grain
Degree uniform results
Claims (7)
1. overflow fineness appreciates a fall fall cyclone bar shaped unit integrated technology such as one liter of nothing, it is characterised in that slurry or treat point
Level slurry is by respectively enteing every point of pipe (6) again after slurry pump pressure (11) press-in pulp-inlet pipe (15), slurry to be fractionated is by every
Root divide pipe (6) distribute to by several Φ 660mm without etc. in fall cyclone (1) the bar shaped unit that constitutes without etc. fall cyclone top
Each charging aperture, the desilting product that fall cyclone such as each nothing (1) obtains is flowed into sand setting mixing machine (8) by sand-precipitating tube (4),
Return to one section of ball mill through desilting discharge pipe (14) regrind；The overflow product that fall cyclone such as each nothing (1) obtain is through overflow
Pipe (16) enters U-shaped overflow launder (2), and U-shaped overflow launder (2) again collects in overflow through overflow discharge header (13) after collecting and mixes
Hopper (10), it is simple to overflow intermediate products sample, overflow intermediate products enter two-stage nitration mill ore discharge slag through overflow batch mixing outlet again
After stock pump pump pond mixes with Secondary grinding mill ore discharge, last overflow intermediate products are again by there being Pulp pump to be pumped to by several Φ
500mm without etc. in the bar shaped unit that constitutes of fall cyclone the fall cyclone upper feed inlet such as each nothing process.
Bar shaped unit integrated technology the most according to claim 1, is characterized in that 4 Φ of described first paragraph classifying equipoment
660mm without etc. fall cyclone form integrated bar shaped unit be to assemble by two row or the horizontally-arranged arrangement mode of three row；Described Φ
660mm is without waiting fall cyclone bar shaped machine component employing 2 for 2 forms, then rotation drops in the fall such as 2 Zhi Wu cyclone operation, other 2 Zhi Wu etc.
Stream device standby mode.
3., according to the bar shaped unit integrated technology described in claims 1, it is characterized in that 6 Φ of described second segment classifying equipoment
500mm without etc. fall cyclone form integrated bar shaped unit be to assemble by two row or the horizontally-arranged arrangement mode of three row；Described Φ
500mm is without waiting fall cyclone bar shaped unit employing 4 for 2 forms, then eddy flow drops in the fall such as 4 Zhi Wu cyclone operation, other 2 Zhi Wu etc.
Device standby mode, point slurry epigranular.
Bar shaped unit integrated technology the most according to claim 1 and 2, is characterized in that using in described first paragraph classifying equipoment
Φ 660mm without etc. fall cyclone be by stock inlet (5), outer overflow adpting flange (2), enter slurry (7), cover plate (3), interior overflow
(6), (11), sand setting nozzle (13) composition, its type of attachment are bored in outer overflow pipe (1), pressure release pipe (15), cylinder cone (9), separation
For, stock inlet (5) is overall structure with entering slurry (7), cover plate (3) with enter slurry (7) use cover plate adpting flange (4) be connected,
Interior overflow (6) and cover plate (3) use tapering to insert outer overflow adpting flange (2) and compress, outside outer overflow (1) uses with cover plate (3)
Overflow adpting flange (2) connects, outer overflow pipe (1) is connected by outer overflow anchor ear (14) each other and connects, pressure release pipe
(15) with outer overflow pipe (1) be overall structure, cylinder cone (9) with enter slurry (7) use cylinder cone adpting flange (8) is connected, divide
Separating cone anchor ear (10) from cone (11) with cylinder cone (9) employing to connect, desilting tip (13) uses desilting tip to embrace with separating cone (11)
Hoop (12) connects, and pressure release pipe (15) is arranged on outer overflow pipe (1) sidepiece and communicates with outer overflow pipe (1).
Bar shaped unit integrated technology the most according to claim 1 and 2, is characterized in that using in described second segment classifying equipoment
Φ 500mm without etc. fall cyclone be by stock inlet (5), enter slurry (7), cover plate (3), interior overflow (6), outer overflow pipe (1), pressure
Power release pipe (15), cylinder cone (9), separation cone (11), sand setting nozzle (13) composition.Its type of attachment is, stock inlet (5) with enter slurry
Body (7) be overall structure, cover plate 3 and enter slurry (7) use cover plate adpting flange (4) be connected, interior overflow (6) is adopted with cover plate (3)
Outer overflow adpting flange (2) is used to be connected with tapering insertion outer overflow adpting flange (2) compression, outer overflow (1) with cover plate (3),
Outer overflow pipe (1) is connected by the connection of outer overflow anchor ear (14), pressure release pipe (15) with outer overflow pipe (1) each other for overall
Structure, cylinder cone (9) uses cylinder cone adpting flange (8) to be connected with entering slurry (7), separates cone (11) and uses with cylinder cone (9)
Separate cone anchor ear (10) connection, desilting tip (13) and separate cone (11) employing desilting tip anchor ear (12) connection, pressure release pipe
(15) outer overflow pipe (1) sidepiece it is arranged on.And communicate with outer overflow pipe (1).
Bar shaped unit integrated technology the most according to claim 4, it is characterized in that described first paragraph classifying equipoment Φ 660mm without
Deng fall cyclone according to cyclone contour stealth be converted into inward eddy operation principle design separation cone long measure L=215mm～
235mm, accounts for the 17.66% of total long 1331mm of cylinder cone.
Bar shaped unit integrated technology the most according to claim 5, it is characterized in that described second segment classifying equipoment Φ 500mm without
Deng fall cyclone be based on cyclone contour stealth be converted into inward eddy operation principle design, its separate cone long measure L=188～
200mm, accounts for the 18.46% of total cylinder cone length 1083mm.
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| CN201610756169.9A CN106179785B (en) | 2016-08-29 | 2016-08-29 | One liter of one drop of overflow fineness appreciation drops cyclone bar shaped unit integrated technology without equal |
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| CN106179785A true CN106179785A (en) | 2016-12-07 |
| CN106179785B CN106179785B (en) | 2019-06-21 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20200305382A1 (en) * | 2017-12-19 | 2020-10-01 | Tetra Laval Holdings & Finance S.A. | Separator and a method for separating milk |
| CN112058512A (en) * | 2020-08-18 | 2020-12-11 | 铜陵有色金属集团股份有限公司 | Blockage monitoring device of sorting equipment and control method thereof |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11207213A (en) * | 1998-01-22 | 1999-08-03 | Cnk:Kk | Hydrocyclone apparatus provided with mechanism for preventing capacity lowering |
| CN2678776Y (en) * | 2004-03-19 | 2005-02-16 | 孙克勤 | Combined grout cyclone separator |
| CN1994580A (en) * | 2006-12-27 | 2007-07-11 | 沈阳铝镁设计研究院 | Silicon removing process for dressing low-grade magnesite |
| CN102921523A (en) * | 2012-12-03 | 2013-02-13 | 云南磷化集团有限公司 | Method for improving grinding efficiency and classification efficiency |
| CN103949356A (en) * | 2014-05-19 | 2014-07-30 | 云南磷化集团有限公司 | Tube-cone connected body hydrocyclone without traditional overflow pipe |
| CN105396705A (en) * | 2015-12-11 | 2016-03-16 | 云南磷化集团有限公司 | Equal-terminal-velocity-free hydrocyclone |
-
2016
- 2016-08-29 CN CN201610756169.9A patent/CN106179785B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11207213A (en) * | 1998-01-22 | 1999-08-03 | Cnk:Kk | Hydrocyclone apparatus provided with mechanism for preventing capacity lowering |
| CN2678776Y (en) * | 2004-03-19 | 2005-02-16 | 孙克勤 | Combined grout cyclone separator |
| CN1994580A (en) * | 2006-12-27 | 2007-07-11 | 沈阳铝镁设计研究院 | Silicon removing process for dressing low-grade magnesite |
| CN102921523A (en) * | 2012-12-03 | 2013-02-13 | 云南磷化集团有限公司 | Method for improving grinding efficiency and classification efficiency |
| CN103949356A (en) * | 2014-05-19 | 2014-07-30 | 云南磷化集团有限公司 | Tube-cone connected body hydrocyclone without traditional overflow pipe |
| CN105396705A (en) * | 2015-12-11 | 2016-03-16 | 云南磷化集团有限公司 | Equal-terminal-velocity-free hydrocyclone |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20200305382A1 (en) * | 2017-12-19 | 2020-10-01 | Tetra Laval Holdings & Finance S.A. | Separator and a method for separating milk |
| CN112058512A (en) * | 2020-08-18 | 2020-12-11 | 铜陵有色金属集团股份有限公司 | Blockage monitoring device of sorting equipment and control method thereof |
| CN112058512B (en) * | 2020-08-18 | 2024-02-06 | 铜陵有色金属集团股份有限公司 | Control method of blockage monitoring device of sorting equipment |
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| CN106179785B (en) | 2019-06-21 |
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