CN1613563A - Composite flashing magnetic field concentration upgrading apparatus - Google Patents
Composite flashing magnetic field concentration upgrading apparatus Download PDFInfo
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- CN1613563A CN1613563A CN 200310103252 CN200310103252A CN1613563A CN 1613563 A CN1613563 A CN 1613563A CN 200310103252 CN200310103252 CN 200310103252 CN 200310103252 A CN200310103252 A CN 200310103252A CN 1613563 A CN1613563 A CN 1613563A
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- refiner
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- 239000002131 composite material Substances 0.000 title 1
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 21
- 239000011707 mineral Substances 0.000 claims description 21
- 150000001875 compounds Chemical class 0.000 claims description 15
- 238000005054 agglomeration Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 11
- 230000008569 process Effects 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 8
- 230000000087 stabilizing effect Effects 0.000 claims description 5
- 229910001220 stainless steel Inorganic materials 0.000 claims description 5
- 239000010935 stainless steel Substances 0.000 claims description 5
- 229910001369 Brass Inorganic materials 0.000 claims description 4
- 239000010951 brass Substances 0.000 claims description 4
- 230000035515 penetration Effects 0.000 claims description 4
- 238000005538 encapsulation Methods 0.000 claims description 3
- 230000002787 reinforcement Effects 0.000 claims description 3
- 230000005672 electromagnetic field Effects 0.000 abstract description 2
- 238000007670 refining Methods 0.000 abstract 1
- 239000012141 concentrate Substances 0.000 description 18
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 230000005484 gravity Effects 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 230000002776 aggregation Effects 0.000 description 9
- 230000001174 ascending effect Effects 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 7
- 239000012535 impurity Substances 0.000 description 7
- 229910052742 iron Inorganic materials 0.000 description 6
- 230000008859 change Effects 0.000 description 5
- 238000005188 flotation Methods 0.000 description 5
- 230000015271 coagulation Effects 0.000 description 4
- 238000005345 coagulation Methods 0.000 description 4
- 229910001608 iron mineral Inorganic materials 0.000 description 3
- 230000005389 magnetism Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000003814 drug Substances 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 206010034719 Personality change Diseases 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 230000005426 magnetic field effect Effects 0.000 description 1
- 239000006249 magnetic particle Substances 0.000 description 1
- 239000006148 magnetic separator Substances 0.000 description 1
- 230000005415 magnetization Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
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- Manufacture And Refinement Of Metals (AREA)
Abstract
A combined ore refiner with flash magnetic field combining permanent magnetic field with electromagnetic field features that its upper cylindrical unit is based on the principle for magnetic conglobation refiner, where the magnetic ore is conglobated, dispersed and conglobated for magnetically pulling it downward, and its lower cylindrical-conic unit is based on the principle of magnetic dewatering trough for further refining. It has automatic control unit for optimal running state.
Description
Technical field
The present invention relates to magnet mineral process technology, especially relate to a kind of selected technical equipment of magnet mineral that carries out.
Background technology
The height direct relation of iron ore concentrate quality the cost of blast furnace process, and ore dressing circle both at home and abroad is improving the emphasis of concentrate grade as scientific research.Mix the intergrowth and the small amounts of monomer gangue of some iron minerals and gangue mineral in the iron ore concentrate that common magnetic plant is selected inevitably, how this part intergrowth and gangue are dished out, be to perplex a difficult problem of respectively selecting factory to improve iron concentrate grade always." reverse flotation " though effectively, complex process, production cost is too high; Magnetic agglomeration gravity separator can only be deviate from fine fraction intergrowth and gangue, can't will deviate from than coarse fraction impurity, and water consumption is big, and operation easier is big.
" reverse flotation " technology is on the basis of fine grinding, and magnetic concentrate is increased reverse flotation work, rejects the lean intergrowth in the concentrate.This technology is complex process not only, require standard higher to granularity and slurry temperature, need to build the reverse flotation factory building, and the iron mineral granularity had strict requirement, and increased consumption such as medicament, power, improved ratio of concentration, reduced production efficiency, increase metal loss, caused production cost to raise, and because made from medicament may cause the influence of environment.
Magnetic agglomeration gravity separator is the patented product (patent No. 85 1 03457.8) by the cooperation design of three units such as The Inst. of Comprehensive Utilization of Mineral Resource, Ministry of Geology and Shoudu Iron and Steel Co. in 1985, be to lean on the magnetic coagulation of suitable control and reinforcement magnetic mineral to be used for realizing, in magnetic agglomeration gravity separator, constituted magnetic field distribution low-intensity magnetic field relatively uniformly by permanent magnetic system, the magnetic field intensity of each point is constant, a magnetic field force magnetize agglomeration, sorting depends primarily on the contrast of the floating lifting force size of gravity and rising flow of slurry.This equipment does not have downward magnetic force, and ascending current can not be too fast, and coarse grain impurity does not take off; Constitute by permanent magnet owing to each magnet ring again, magnetic field exists all the time, " reunion-dispersion-reunion " phenomenon that magnetic mineral only depends on more weak magnetic field force and gravity to form in ore pulp is not obvious, the impurity that is mingled with is difficult for taking off, when especially lean intergrowth content was higher in ore, sorting result was more undesirable; In addition, this equipment volume is huge, and water consumption is very big, makes that the burden of the water yield increases in the flow process, has increased the burden of pump and magnetic separator; The technology operation is adjusted complicated, needs more experienced post operation worker just can adjust, otherwise will cause the fluctuation of mineral processing index.
Summary of the invention
The objective of the invention is for the magnet mineral are sorted, especially carry out selected, defective and deficiency at " reverse flotation " technology and magnetic agglomeration gravity separator existence have proposed a kind of compound flicker of wet type picking equipment magnetic field refiner by magnetic force, gravity and hydraulic forces.
The present invention includes cylindrical shell, ore feeder, overflow launder, feed feeder, ore discharge valve, it is characterized in that: be provided with the plurality of electromagnetic coil that is submerged in the ore pulp from top to bottom at regular intervals at cylinder inboard wall, being provided with permanent magnet in the feed feeder bottom evenly distributes along circumference, point to the center of circle with pole-face, the solenoid of topmost is powered continuously, and by the Current Control electromagnetism intensity, to keep the overflow liquid level stabilizing; The bottom solenoid is intermittence, power supply at interval successively from top to bottom, produces flicker magnetic field, and the reinforcement magnetic mineral produces reunion-dispersion-agglomeration in ore pulp; Detect the confluent signal by flowmeter, detect with pressure sensor and divide the constituency concentration signal,, meet setting value and overflow liquid level stabilizing to keep confluent by the current strength of control system control magnetic valve and ore discharge valve and solenoid.
Solenoid is by waterproof, Wear-resistant Treatment, and the cable penetration pipe directly is placed in the ore pulp and works through encapsulation process.Solenoid top array solenoid is big coil, and bottom array solenoid is a small coil.Permanent magnet is fixed on along on the circumferential inner wall ring-type stainless steel band with brass bolt.
Advantage of the present invention is to have concentrated the characteristics that sort of magnetic agglomeration gravity separator and permanent-magnet drench pit, designed special magnetic signature, equipment itself can be controlled automatically, not only can effectively the particulate impurity in the iron ore concentrate be dished out, and can effectively more coarsely graded intergrowth and gangue mineral be dished out, reach the purpose that increases substantially concentrate grade.Commerical test proves that its amplitude that improves concentrate grade is higher 2～3 times than magnetic agglomeration gravity separator.
Description of drawings
Fig. 1 is a compound flicker magnetic field refiner structural representation involved in the present invention;
Fig. 2 is an A-A profile among Fig. 1.
As shown in the figure: 1. ore feeder, 2. pressure sensor, 3. overflow launder, 4. cylindrical shell, 5. cable penetration pipe, 6. coil brace, 7. big solenoid, 8. little solenoid, 9. feed feeder, 10. permanent magnet, 11. YE, 12. magnetic valves, 13. flowmeters, 14. ore discharge valves.
The specific embodiment
Close the structure of the compound flicker of the present invention magnetic field refiner and position: overflow launder 3 is installed in cylindrical shell 4 tops, downflow weir place setting pressure sensor 2, ore feeder 1 is supported on the overflow launder 3, mineral-feeding pipe tangentially feeds, top is provided with blast pipe, the bottom mineral-feeding pipe is deep into cylindrical shell 4 inside and gives the ore deposit by the middle part level, and the mineral-feeding pipe bottom is provided with the dish of returning mine.Feed feeder 9 is arranged on cylindrical shell 4 bottom cones top, and flowmeter 13 and magnetic valve 12 are installed on the supply line, and feed feeder 9 water pipe that respectively feeds water all tangentially feeds cylindrical shell 4 to water, in cylinder center a feed pipe is set downwards, and returns water pond.In the cylindrical shell bottom, ore discharge valve 14 is installed, control the opening degree of ore discharge valve 14 with YE 11, finally control concentrate ore discharge amount.
This refiner inside is provided with electromagnetic permanent magnet combined magnetic, wherein feed feeder 9 bottoms are fixed with permanent magnet 10 and evenly distribute along circumference, be fixed on along on the circumferential inner wall ring-type stainless steel band with brass bolt, point to the center of circle with pole-face, be provided with the plurality of electromagnetic coil 7,8 that is submerged in the ore pulp from top to bottom at regular intervals at cylinder inboard wall, coil is placed on the coil brace made from stainless steel that is easy to dismantle 6, the solenoid of topmost is powered continuously, and by the Current Control electromagnetism intensity, to keep the overflow liquid level stabilizing.Several groups of solenoids in bottom are intermittence, power supply at interval successively from top to bottom, produces flicker magnetic field.It is attached with automatic control system that this invents compound flicker magnetic field refiner, wherein: detect the confluent signal by flowmeter 13, detect branch constituency concentration signal with pressure sensor 2, by the current strength of control system control magnetic valve 12, ore discharge valve 14 and solenoid 7,8, to keep confluent to meet setting value and the overflowing liquid surface state is stable.
The operating principle of the compound flicker of the present invention magnetic field refiner is: compound flicker magnetic field refiner utilizes magnet exciting coil to generate an electromagnetic field, and has improved the sorting condition of fine fraction magnetite ore particles, improves separating effect.Ore pulp is fed in the cylindrical shell by ore feeder, and the magnetization in the flicker magnetic field that is produced by solenoid of Armco magnetic iron mineral forms the magnetic coagulation body, has strengthened own wt and has added magneticaction, has overcome the downward sedimentation of floating act effect of the ascending current that is fed by feed feeder.In the infall process, be continuous reunion-loose-aggregating state, so that the gangue mineral and the more weak intergrowth water of magnetic that are mingled with in the aggregate are gone out, make concentrate constantly obtain purifying, when concentrate is deposited to the feed feeder below, be subjected to the effect of the advanced magnetic dewater cone that constitutes by permanent magnetic system and conical section again, further selected, form final concentrate and from the ore discharge valve of bottom, discharge.Gangue mineral and intergrowth do not overcome the ascending current effect, move upward with ascending water, form overflow at last and discharge from overflow launder.In the process that moves upward, the magnetic field of constantly being glimmered again acts on, with the iron ore concentrate reunion sinking of monomer dissociation.
When mine-supplying quantity and confluent change, in cylinder, put then variation thereupon of (title selects subregion) concentration between the downflow weir to the ore deposit, pressure sensor is passed to automaton with the change in concentration signal, current strength by automaton control solenoid, magnetic field intensity is also changed thereupon, thereby change the magnetic mineral subsidence velocity, also control simultaneously the opening degree of following ore discharge valve, change ore discharge speed, detect the flow meter signal size by automatic control system again, the control magnetic valve is adjusted confluent, thereby keeps selecting subregion concentration to be tending towards setting value, keeps the best and sorts state.When ore character changes, during the concentrate quality fluctuation, then adjust current setting value, make magnetic field intensity adapt to ore and change, guarantee the final concentrate quality, realization is selected to magnetic mineral.
The characteristics of the compound flicker of the present invention magnetic field refiner are:
This invents compound flicker magnetic field refiner improves the unit platform by the electromagnetism magnetic field that makes full use of the solenoid generation disposal ability.Consider to give influence of various factors such as ore deposit mode and processing ore pulp amount, seven groups of solenoids insulative water-proof, Wear-resistant Treatment have been carried out, cable carries out encapsulation process at cable penetration pipe place, solenoid directly is placed in the ore pulp works, disposal ability increases substantially, and has both reached to reduce the purpose that configuration is installed, the platform number is started in minimizing, has saved investment amount and operation consumption, simplify device structure again, be convenient to maintenance.
This is invented compound flicker magnetic field refiner the cylindrical portions may of magnetic agglomeration gravity separator (sorting the district) is combined on the permanent-magnet drench pit of top magnetic system, and changes the magnetic system of magnetic agglomeration gravity separator into electromagnetism by permanent magnetism.Magnetic system is placed on cylinder interior, and bottom magnetic is permanent magnetic system, is to be uniformly distributed along the circumference by permanent magnets to constitute, and is fixed on along on the circumferential inner wall ring-type stainless steel band with brass bolt, points to the center of circle with pole-face.Its residual magnetism system constitutes by solenoid, has so just formed a compound magnetic that is made of solenoid and permanent magnets to be.Wherein solenoid is totally 7, and the 4 groups of solenoids in top are big coil, and the 3 groups of solenoids in bottom are small coil, at interval 200～250mm.Above 4 coil turns more, spacing is less, with produce higher magnetic field intensity (because of this district's ascending current speed big); Below 3 coil turns less, spacing is bigger.The coil in top is powered continuously, and purpose is to protect spillwag chute to stablize, and " does not turn over the black ore deposit of running ".Other coil is pressed certain hour order intermittence, power supply at interval successively, to produce flicker magnetic field, makes magnetic mineral produce sufficient reunion-dispersion-agglomeration in ore pulp.The current strength of power supply, power-on time, intermittent time and interval coil number are all adjustable.
Because of coil is pressed order power supply successively up and down, guaranteed that magnetic mineral is subjected to downward magneticaction all the time in infall process, on the basis of magnetic coagulation technology, make the magnetite concentrate mineral grain on the basis that is subjected to the gravity effect, be subjected to the effect of a downward magnetic field force again; Again because of coil spacing, intermittent power supply, after magnetic mineral is reunited enough dispersion space are arranged in ore pulp, promote intergrowth and gangue fully to break away from aggregate, so can carry out the interpolation of the ascending water water yield fully, can be when the magnetic coagulation body disperses, intergrowth and gangue mineral are fully deviate from, and taken to the top by ascending current and go out from the overflow longshore current.The cylindrical shell top diameter shrinks, and sectional area reduces, and ascending current speed is accelerated, and discharges with overflow as early as possible so that break away from the impurity in magnetic field.Finally reach not only and can effectively deviate from particulate impurity in the concentrate, can fully take off purpose again than coarse fraction impurity.
Cylinder below the feed feeder and conical section are equivalent to the advanced magnetic dewater cone of permanent magnetism of a top magnetic system.From top to bottom, the concentration and the proportion of each point ore pulp progressively strengthen, and less gangue of proportion and intergrowth further are eliminated, and selected effect is stronger.
Automatically regulate magnetic field intensity, improved the adaptivity that sorts.Can adjust according to the variation of pulp density for the magnetic field intensity that coil is produced, improve its adaptivity.Set up concentration detection apparatus in a minute constituency, adjust electric current in the coil by the concentration that detects the branch constituency, when the concentration in minute constituency increases, strengthen the electric current of coil, increase the active force of magnetic field, prevent that mineral powder granular from can not overcome the scouring force of current and to cause overflow to turn over black magnetic conduction particle in the ore pulp; When the concentration in minute constituency reduces, by reducing the electric current in the coil, reduce magnetic field intensity and prevent that magnetic-particle in the ore pulp from because conglomerate is too magnetized in excessive magnetic field effect, can't open again, and influencing sorting result after magnetic field disappears.The realization of this requirement is a passing ratio, integration, derivative controller is that PID realizes, at the inner liquid level difference meter of installing of Electromagnetic accumulating machine, detect the variable signal of the pulp density that self-supporting mining area makes progress by liquid level sensor, the electric current that is converted into 4～20mA of standard is sent into the PID controller, automatically export 8031 singlechip control panels to by setting P (ratio) I (integration) D (differential) parameter and setting value parameter S V, 8031 control panels are regulated output again circulation silicon controlled control voltage are controlled the electric current of coil in the circulation magnetic field and the opening degree of bottom ore discharge valve.In addition, flowmeter and magnetic valve are housed on the feed feeder supply channel, detect water yield signal,, keep confluent to meet duty setting signal by the open degree of PID control magnetic valve by flowmeter.This has just guaranteed that equipment is in the best all the time and sorts state, and without the manually-operated adjustment.
Claims (4)
1. compound flicker magnetic field refiner, comprise cylindrical shell, ore feeder, overflow launder, feed feeder, ore discharge valve, it is characterized in that: be provided with plurality of electromagnetic coil (7), (8) that are submerged in the ore pulp from top to bottom at regular intervals at cylindrical shell (4) inwall, being provided with permanent magnet (10) in described feed feeder (9) bottom evenly distributes along circumference, point to the center of circle with pole-face, the solenoid of topmost is powered continuously, and by the Current Control electromagnetism intensity, to keep the overflow liquid level stabilizing; Bottom solenoid (7), (8) are intermittence, power supply at interval successively from top to bottom, produces flicker magnetic field, and the reinforcement magnetic mineral produces reunion-dispersion-agglomeration in ore pulp; Detect the confluent signal by flowmeter (13), detect branch constituency concentration signal with pressure sensor (2), by the current strength of control system control magnetic valve (12), ore discharge valve (14) and solenoid (7), (8), meet setting value and overflow liquid level stabilizing to keep confluent.
2. a kind of compound flicker according to claim 1 magnetic field refiner is characterized in that: solenoid (7), (8) are by waterproof, Wear-resistant Treatment, and cable penetration pipe (5) directly is placed in the ore pulp and works through encapsulation process.
3. a kind of compound flicker according to claim 1 magnetic field refiner, it is characterized in that: described solenoid top array solenoid (7) is big coil, and bottom array solenoid (8) is a small coil.
4. a kind of compound flicker according to claim 1 magnetic field refiner, it is characterized in that: described permanent magnet (10) is fixed on along on the circumferential inner wall ring-type stainless steel band with brass bolt, also can be solenoid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2003101032529A CN100444965C (en) | 2003-11-04 | 2003-11-04 | Composite flashing magnetic field concentration upgrading apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2003101032529A CN100444965C (en) | 2003-11-04 | 2003-11-04 | Composite flashing magnetic field concentration upgrading apparatus |
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| Publication Number | Publication Date |
|---|---|
| CN1613563A true CN1613563A (en) | 2005-05-11 |
| CN100444965C CN100444965C (en) | 2008-12-24 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB2003101032529A Expired - Fee Related CN100444965C (en) | 2003-11-04 | 2003-11-04 | Composite flashing magnetic field concentration upgrading apparatus |
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| CN (1) | CN100444965C (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102159320A (en) * | 2008-09-18 | 2011-08-17 | 西门子公司 | Device for separating ferromagnetic particles from a suspension |
| CN101219413B (en) * | 2008-01-22 | 2013-04-10 | 福州昌晖自动化系统有限公司 | Technique for manufacturing hyperpure iron extract |
| CN104772211A (en) * | 2015-04-30 | 2015-07-15 | 山东华特磁电科技股份有限公司 | Electromagnetic elutriation fine separation machine |
| CN107890950A (en) * | 2015-10-27 | 2018-04-10 | 张荣斌 | A kind of automatic control system of mine magnetic separator |
| CN112427139A (en) * | 2020-10-14 | 2021-03-02 | 清华大学 | Magnetic liquid screening device |
| CN113457264A (en) * | 2021-06-29 | 2021-10-01 | 云南大红山管道有限公司 | Method and device for adjusting grading of iron concentrate slurry conveyed by pipeline, and method and device for filtering iron concentrate slurry |
| CN113552510A (en) * | 2021-06-29 | 2021-10-26 | 云南大红山管道有限公司 | Magnetism increasing experimental device and method for iron ore concentrate pulp |
| CN113695081A (en) * | 2021-08-24 | 2021-11-26 | 北矿机电科技有限责任公司 | Separator of electric permanent magnet |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4316542A (en) * | 1980-07-15 | 1982-02-23 | Zelenov Petr I | Electromagnetic separator |
| US4317719A (en) * | 1980-10-06 | 1982-03-02 | Tomotoshi Tokuno | Wet-type magnetic ore separation apparatus |
| CN85103457B (en) * | 1985-05-10 | 1988-02-24 | 首都钢铁公司 | Magnetic agglomeration gravity separation method and the separator |
| US5868255A (en) * | 1996-09-03 | 1999-02-09 | Mcgaa; John R. | Alternating current magnetic separator |
| CN2323874Y (en) * | 1998-03-31 | 1999-06-16 | 攀钢集团矿业公司 | Magnetic separator |
| JP2001212476A (en) * | 2000-01-31 | 2001-08-07 | Nippon Magnetic Dressing Co Ltd | Method for recovering valuable material from used graphite-containing refractory brick |
-
2003
- 2003-11-04 CN CNB2003101032529A patent/CN100444965C/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101219413B (en) * | 2008-01-22 | 2013-04-10 | 福州昌晖自动化系统有限公司 | Technique for manufacturing hyperpure iron extract |
| CN102159320A (en) * | 2008-09-18 | 2011-08-17 | 西门子公司 | Device for separating ferromagnetic particles from a suspension |
| CN102159320B (en) * | 2008-09-18 | 2013-06-19 | 西门子公司 | Device for separating ferromagnetic particles from a suspension |
| CN104772211A (en) * | 2015-04-30 | 2015-07-15 | 山东华特磁电科技股份有限公司 | Electromagnetic elutriation fine separation machine |
| CN104772211B (en) * | 2015-04-30 | 2019-02-19 | 山东华特磁电科技股份有限公司 | Electromagnetism eluriates refiner |
| CN107890950A (en) * | 2015-10-27 | 2018-04-10 | 张荣斌 | A kind of automatic control system of mine magnetic separator |
| CN112427139A (en) * | 2020-10-14 | 2021-03-02 | 清华大学 | Magnetic liquid screening device |
| CN112427139B (en) * | 2020-10-14 | 2021-09-07 | 清华大学 | Magnetic liquid screening device |
| CN113457264A (en) * | 2021-06-29 | 2021-10-01 | 云南大红山管道有限公司 | Method and device for adjusting grading of iron concentrate slurry conveyed by pipeline, and method and device for filtering iron concentrate slurry |
| CN113552510A (en) * | 2021-06-29 | 2021-10-26 | 云南大红山管道有限公司 | Magnetism increasing experimental device and method for iron ore concentrate pulp |
| CN113695081A (en) * | 2021-08-24 | 2021-11-26 | 北矿机电科技有限责任公司 | Separator of electric permanent magnet |
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| CN100444965C (en) | 2008-12-24 |
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Address after: 100041 Beijing Shijingshan District Shougang Corporation Patentee after: SHOUGANG GROUP Co.,Ltd. Address before: 100041 Beijing Shijingshan District Shougang Corporation Patentee before: SHOUGANG Corp. |
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Granted publication date: 20081224 |