CN101757986A - Method for floating bauxite - Google Patents
Method for floating bauxite Download PDFInfo
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- CN101757986A CN101757986A CN200910243351A CN200910243351A CN101757986A CN 101757986 A CN101757986 A CN 101757986A CN 200910243351 A CN200910243351 A CN 200910243351A CN 200910243351 A CN200910243351 A CN 200910243351A CN 101757986 A CN101757986 A CN 101757986A
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- concentrate
- ore
- froth
- pulp
- foam
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- 229910001570 bauxite Inorganic materials 0.000 title claims abstract description 29
- 238000000034 method Methods 0.000 title claims abstract description 27
- 238000007667 floating Methods 0.000 title claims abstract description 19
- 239000012141 concentrate Substances 0.000 claims abstract description 42
- 238000000227 grinding Methods 0.000 claims abstract description 27
- 239000002893 slag Substances 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000006260 foam Substances 0.000 claims description 36
- 238000005188 flotation Methods 0.000 claims description 23
- 239000003795 chemical substances by application Substances 0.000 claims description 15
- 230000000694 effects Effects 0.000 claims description 15
- 210000004027 cell Anatomy 0.000 claims description 12
- 239000007921 spray Substances 0.000 claims description 7
- 238000012545 processing Methods 0.000 claims description 4
- 210000005056 cell body Anatomy 0.000 claims description 2
- 238000007790 scraping Methods 0.000 claims description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract description 5
- 238000004131 Bayer process Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000001914 filtration Methods 0.000 abstract 2
- 239000000463 material Substances 0.000 abstract 1
- 230000002000 scavenging effect Effects 0.000 abstract 1
- 230000005540 biological transmission Effects 0.000 description 9
- 239000000203 mixture Substances 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 7
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000002002 slurry Substances 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 3
- 239000002270 dispersing agent Substances 0.000 description 3
- 235000021321 essential mineral Nutrition 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- KMWBBMXGHHLDKL-UHFFFAOYSA-N [AlH3].[Si] Chemical compound [AlH3].[Si] KMWBBMXGHHLDKL-UHFFFAOYSA-N 0.000 description 1
- 230000004308 accommodation Effects 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229910001648 diaspore Inorganic materials 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000010334 sieve classification Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
The invention relates to a method for floating bauxite, which is characterized in that: a froth product of grinding and rough concentration enters a pulp filtering tank and the enriched mineralized froth floats on the surface of ore pulp and overflows from the overflow opening of the pulp filtering tank to give a concentrate I; the defrothed impure ore pulp flows downwards, bottom-flow ore pulp enters a concentrating and floating tank under the action of a slag pulp pump, and a froth product of the concentration is used as a concentrate II; the bottom flow of the concentration returns to rough concentration operation, the bottom flow of the rough concentration is scavenged, the froth of the scavenged returns to the rough concentration operation, and the bottom flow of the scavenging is used as tailings; and the concentrate I and the concentrate II are combined to form the final concentrate. The method of the invention effectively solves the froth transport problem, stabilizes the ore pressure of the ore pulp feed and the floatation process, reduces the water consumption of the floatation system, improves floatation concentration, reduces the floatation time of qualified concentrate, improves equipment capacity, improves ore dressing indexes, reduces production cost and provides qualified bauxite concentrate material for the Bayer-process production of alumina.
Description
Technical field
A kind of bauxite floating method relates to a kind of method to the bauxite flotation desiliconization.
Background technology
China's bauxite reserves are abundant, but 80% be in low-grade diaspore type bauxite, can not directly adopt the bayer process of economical and efficient to produce aluminium oxide, need to improve the bauxite aluminium-silicon ratio through pre-desiliconization.Along with the high speed development of aluminium industry, cause the high-quality bauxite resource sharply to reduce, flotation desilication becomes more and more important as effective, the most economic method for desilication.The grade of ore descends, and the technology of ore dressing is variation immediately, and the advantage of the direct-flotation desiliconisation technology of bauxite is also more obvious, but float-amount is big, foam viscosity greatly still is its feature.
The no transmission floatation process technology of studying now and promoting gradually mainly adopts pump and gases at high pressure to strengthen gas-liquid mixed, high turbulent condition mineralising, low turbulent condition sorting have been realized, strengthened the particulate mineralising, mineralising is effective, reduce the mixing and the interference of concentrate and tailings, improved the efficiency of separation greatly.Therefore, this kind equipment accommodation is extensive, sorting thick, fine all is fit to, coarse grain is carried out quick collecting, simultaneously can strengthen the collecting fine mineral, energy-conservation in addition (energy-conservation 30%), dosing few (collector dosage reduces by 30%), floor space are little, small investment and advantages of simple structure and simple.
Because the bauxite forward flotation foam is many, and it is more sticking, to cross the slurry bucket through one because roughly select foam, enter by the slag stock pump then selected, in order to guarantee floatation concentration, control washing water quantity, may cause the transmission of foam not smooth, comprise that the foam delivery pump is easy to occur not even situation such as dnockout of " cavitation erosion ", inefficiency, thereby the ore deposit pressure and the flow process that influences pan feeding be stablized, influence separation index, foam occurs roughly selecting and transmit insoluble problem.
Summary of the invention
The objective of the invention is deficiency at above-mentioned prior art existence, provide a kind of and can effectively solve problems such as the bauxite flotation foam transmits, pan feeding slag stock pump efficient is low, effectively stablize the pan feeding ore deposit and press, shorten flotation process, improve the bauxite floating method of mineral processing index.
The objective of the invention is to be achieved through the following technical solutions.
A kind of bauxite floating method, the processing step of its floatation process comprises: ore grinding, classification, flotation, it is characterized in that after ore pulp behind the ore grinding and floating agent effect, entering and roughly select, the froth pulp of roughly selecting entered stock tank, at the high-grade mineralized froth that obtains the postdigestive more low-grade ore pulp of foam segment under the shower water effect and disappear through the difficulty after the enrichment, mineralized froth after enrichment floats on above the ore pulp, and overflowing from the overfall of crossing stock tank becomes concentrate I; Be mingled with froth breaking after ore pulp toward current downflow, the underflow ore pulp enters selected flotation cell by the slag stock pump, selected froth pulp is as concentrate II; Selected underflow returns roughly selects operation, roughly selects underflow and enters and scan, and scans foam and returns and roughly select operation, scans underflow as mine tailing; Concentrate I, concentrate II merge into final concentrate.
A kind of bauxite floating method of the present invention, it is characterized in that the froth pulp roughly selected to cross stock tank be the container that contains overfall, foam feeder, underflow pipe simultaneously, crossing stock tank is column type, inverted conical type or square cell body, the foam mode of overflowing after enrichment is that foam is from overflowing, or scraping foam by float skimming device, the overfall of crossing stock tank overflows part as concentrate I.
A kind of bauxite floating method of the present invention is characterized in that being provided with spray water system above the stock tank, made water to be on the whole area of crossing stock tank top to spray shape to spray and roughly selected on the foam, washed and was mingled with and further enrichment roughly selecting foam.
Method of the present invention, can effectively solve the foam transmission problem, solve not even problem such as dnockout of " cavitation erosion " that the foam delivery pump occurs, inefficiency, stablizing the ore deposit of ore pulp pan feeding presses, stablize flotation flowsheet, reduce the water content consumption of flotation system, improve floatation concentration, reduce the flotation time of qualified concentrate containing, improve equipment capacity, improve mineral processing index, reduce production costs, for alumina producing Bayer process provides the bauxite concentrate raw material of qualified grade, the low alumina-silicon ratio alumyte resource provides a new approach in China in order efficiently to utilize.
Description of drawings
Fig. 1 is the process chart of the inventive method;
Fig. 2 be stock tank totally show structural representation;
Fig. 3 was the partial schematic diagram of stock tank;
Fig. 4 was the partial schematic diagram of stock tank.
Table 10 has indicated the title of crossing each parts of stock tank.
The specific embodiment
A kind of bauxite floating method, the bauxite raw ore enters the primary grinding machine and roughly grinds, mog for-when 0.074mm accounts for 50%-80%, the ore grinding product through with the floating agent effect after enter into floatation equipment and roughly select, the froth pulp of roughly selecting entered stock tank, at the high-grade mineralized froth that obtains the postdigestive more low-grade ore pulp of foam segment under a certain amount of shower water effect and disappear through the difficulty after the enrichment, mineralized froth after enrichment floats on above the ore pulp, and overflowing from the overfall of crossing stock tank becomes concentrate I; Be mingled with froth breaking after ore pulp toward current downflow, the underflow ore pulp enters selected flotation cell by the slag stock pump, selected froth pulp is as concentrate II; Selected underflow returns roughly selects operation, and the underflow of roughly selecting enters the high-effective classifying equipment, and coarse fraction enters two sections open-circuit grindings, and the ore grinding product returns to be roughly selected; Fine fraction enters scans operation, scans foam and returns and roughly select operation, scans underflow as mine tailing; Concentrate I, concentrate II merge into final concentrate.
Embodiment 1
With the low-grade bauxite of Henan A/S＜3 is the test sample ore, and raw ore main chemical compositions and thing phase composition see Table 1 respectively, table 2.The principle process chart is seen accompanying drawing 1, and the concrete technology of its desiliconization is as follows:
The Henan low-grade bauxite exists with the treating capacity of 2t/h
Grate ball mill in carry out ore grinding, add an amount of sodium carbonate dispersant in the grinding machine, the mog of the ore grinding product that obtains accounts for 78.6% for-0.074mm, the ore grinding product promptly is that classifier overflow enters the raw ore slurry agitator through comprising that with floating agent being driven into flotation cell without transmission by the slag stock pump after 80g/t adjusts the collecting agent effect of agent 400g/t roughly selects, the froth pulp of roughly selecting entered stock tank, at the high-grade mineralized froth that obtains the postdigestive more low-grade ore pulp of foam segment under a certain amount of shower water effect and disappear through the difficulty after the enrichment, mineralized froth after enrichment floats on above the ore pulp, and overflowing from the overfall of crossing stock tank becomes concentrate I; Be mingled with froth breaking after ore pulp toward current downflow, the underflow ore pulp enters selected flotation cell by the slag stock pump, selected froth pulp is as concentrate II; Selected underflow returns roughly selects operation; The underflow of roughly selecting enters
Cyclone classification, cyclone sand setting (fineness for-0.074mm account for 41.0%) enters two sections open-circuit grindings, ore grinding product (fineness for-0.074mm account for 75.0%) returns and roughly selects; Cyclone overflow (fineness for-0.074mm greater than 95%) enters and scans agitator, through with the collecting agent effect of 300g/t after squeeze into flotation cell without transmission by the slag stock pump and scan, scan foam and return and roughly select operation, scan underflow as mine tailing; Concentrate I, concentrate II merge into final concentrate.Its ore dressing and desiliconizing the results are shown in Table 3.
Table 1 raw ore chemical composition complete analysis (%)
The content of essential mineral (%) in table 2 raw ore
Table 3 ore dressing and desiliconizing result
Being about 4.2 low-grade bauxite with Henan A/S is the test sample ore, and raw ore main chemical compositions and thing phase composition see Table 4 respectively, table 5.The principle process chart is seen accompanying drawing 1, and the concrete technology of its desiliconization is as follows:
The Henan low-grade bauxite exists with the treating capacity of 80t/h
Rod mill in carry out ore grinding, add an amount of sodium carbonate dispersant in the grinding machine, the mog of the ore grinding product that obtains accounts for 67.5% for-0.074mm, the ore grinding product promptly is that classifier overflow enters the raw ore slurry agitator through comprising that with floating agent being driven into flotation cell without transmission by the slag stock pump after 80g/t adjusts the collecting agent effect of agent 450g/t roughly selects, the froth pulp of roughly selecting entered stock tank, at the high-grade mineralized froth that obtains the postdigestive more low-grade ore pulp of foam segment under a certain amount of shower water effect and disappear through the difficulty after the enrichment, mineralized froth after enrichment floats on above the ore pulp, and overflowing from the overfall of crossing stock tank becomes concentrate I; Be mingled with froth breaking after ore pulp toward current downflow, the underflow ore pulp enters selected flotation cell by the slag stock pump, selected froth pulp is as concentrate II; Selected underflow returns roughly selects operation; The underflow of roughly selecting enters 1170 * 1670 dither sieve classifications, and sieve top (fineness for-0.074mm account for 28.0%) enters two sections open-circuit grindings, and ore grinding product (fineness for-0.074mm account for 68.6%) returns and roughly selects; Lower part of screen branch (fineness for-0.074mm greater than 98%) enters and scans agitator, through with the collecting agent effect of 200g/t after squeeze into flotation cell without transmission by the slag stock pump and scan, scan foam and return and roughly select operation, scan underflow as mine tailing; Concentrate I, concentrate II merge into final concentrate.Its ore dressing and desiliconizing the results are shown in Table 6.
Table 4 raw ore chemical composition complete analysis (%)
The content of essential mineral (%) in table 5 raw ore
Table 6 ore dressing and desiliconizing result
Being about 5.7 low-grade bauxite with Shanxi Jin Nan A/S is the test sample ore, and raw ore main chemical compositions and thing phase composition see Table 7 respectively, table 8.The principle process chart is seen accompanying drawing 1, and the concrete technology of its desiliconization is as follows:
The Henan low-grade bauxite exists with the treating capacity of 2.1t/h
Grate ball mill in carry out ore grinding, add an amount of sodium carbonate dispersant in the grinding machine, the mog of the ore grinding product that obtains accounts for 56.8% for-0.074mm, the ore grinding product promptly is that classifier overflow enters the raw ore slurry agitator through comprising that with floating agent being driven into flotation cell without transmission by the slag stock pump after 80g/t adjusts the collecting agent effect of agent 300g/t roughly selects, the froth pulp of roughly selecting entered stock tank, at the high-grade mineralized froth that obtains the postdigestive more low-grade ore pulp of foam segment under a certain amount of shower water effect and disappear through the difficulty after the enrichment, mineralized froth after enrichment floats on above the ore pulp, and overflowing from the overfall of crossing stock tank becomes concentrate I; Be mingled with froth breaking after ore pulp toward current downflow, the underflow ore pulp enters selected flotation cell by the slag stock pump, selected froth pulp is as concentrate II; Selected underflow returns roughly selects operation; The underflow of roughly selecting enters
Cyclone classification, cyclone sand setting (fineness for-0.074mm account for 30.8%) enters two sections open-circuit grindings, ore grinding product (fineness for-0.074mm account for 71.0%) returns and roughly selects; Cyclone overflow (fineness for-0.074mm greater than 95%) enters and scans agitator, through with the collecting agent effect of 200g/t after squeeze into flotation cell without transmission by the slag stock pump and scan, scan foam and return and roughly select operation, scan underflow as mine tailing; Concentrate I, concentrate II merge into final concentrate.Its ore dressing and desiliconizing the results are shown in Table 9.
Table 7 raw ore chemical composition complete analysis (%)
The content of essential mineral (%) in table 8 raw ore
Table 9 ore dressing and desiliconizing result
Table 10
| Sequence number | Title |
| 1 | |
| 2 | Scrape the |
| 3 | Foam collecting tank |
| 4 | |
| 5 | Underflow opening |
| 6 | The foam overfall |
| 7 | Cross the stock tank top cover |
| 8 | |
| 9 | |
| 10 | The A-A section |
Claims (3)
1. bauxite floating method, the processing step of its floatation process comprises: ore grinding, classification, flotation, it is characterized in that after ore pulp behind the ore grinding and floating agent effect, entering and roughly select, the froth pulp of roughly selecting entered stock tank, at the high-grade mineralized froth that obtains the postdigestive more low-grade ore pulp of foam segment under the shower water effect and disappear through the difficulty after the enrichment, mineralized froth after enrichment floats on above the ore pulp, and overflowing from the overfall of crossing stock tank becomes concentrate I; Be mingled with froth breaking after ore pulp toward current downflow, the underflow ore pulp enters selected flotation cell by the slag stock pump, selected froth pulp is as concentrate II; Selected underflow returns roughly selects operation, roughly selects underflow and enters and scan, and scans foam and returns and roughly select operation, scans underflow as mine tailing; Concentrate I, concentrate II merge into final concentrate.
2. a kind of bauxite floating method according to claim 1, it is characterized in that the froth pulp roughly selected to cross stock tank be the container that contains overfall, foam feeder, underflow pipe simultaneously, crossing stock tank is column type, inverted conical type or square cell body, the foam mode of overflowing after enrichment is that foam is from overflowing, or scraping foam by float skimming device, the overfall of crossing stock tank overflows part as concentrate I.
3. a kind of bauxite floating method according to claim 1, it is characterized in that being provided with above the stock tank spray water system, make water on the whole area of crossing stock tank top, to be to spray shape to spray and roughly select on the foam, wash and be mingled with and further enrichment roughly selecting foam.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200910243351 CN101757986B (en) | 2009-12-18 | 2009-12-18 | Method for floating bauxite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200910243351 CN101757986B (en) | 2009-12-18 | 2009-12-18 | Method for floating bauxite |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101757986A true CN101757986A (en) | 2010-06-30 |
| CN101757986B CN101757986B (en) | 2013-03-20 |
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Country Status (1)
| Country | Link |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102205275A (en) * | 2011-05-18 | 2011-10-05 | 昆明理工大学 | Reinforced floatation desilicification method for high-silicon bauxite |
| CN102489411A (en) * | 2011-12-26 | 2012-06-13 | 昆明理工大学 | Flotation two-stage desiliconization method for high-silicon bauxite |
| CN102806146A (en) * | 2012-07-27 | 2012-12-05 | 中国铝业股份有限公司 | Method for performing beneficiation and desilicification on bauxite |
| CN103285625A (en) * | 2013-06-13 | 2013-09-11 | 北京矿冶研究总院 | Defoaming method for reverse flotation desilication of phosphorite |
| CN103521363A (en) * | 2013-10-19 | 2014-01-22 | 李耀吾 | Low-quality raw bauxite ore open-grinding and dressing technology |
| CN104841567A (en) * | 2015-06-08 | 2015-08-19 | 河南东大矿业股份有限公司 | Flow mixing method for bauxite forward flotation |
| CN107051711A (en) * | 2017-04-10 | 2017-08-18 | 中国铝业股份有限公司 | A kind of method that mineral processing tailing of bauxite is selected again |
| CN109158221A (en) * | 2018-08-23 | 2019-01-08 | 广东省大宝山矿业有限公司 | A kind of copper sulphur mine ore-sorting system improving foam pump mounting means |
| CN110876988A (en) * | 2019-12-11 | 2020-03-13 | 太原睿孚特选煤技术有限公司 | Circulation volume automatic compensation pan feeding volume fluctuation's cavitation jet microbubble flotation column |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB563045A (en) * | 1941-10-21 | 1944-07-27 | American Cyanamid Co | Improvements in bauxite beneficiation |
| HU167599B (en) * | 1973-11-29 | 1975-11-28 | ||
| AUPQ563800A0 (en) * | 2000-02-15 | 2000-03-09 | University Of Newcastle Research Associates Limited, The | Improved froth flotation process and apparatus |
| CN1125777C (en) * | 2001-06-29 | 2003-10-29 | 中南大学 | Dressing process for desiliconizing bauxite with medium or low Al/Si ratio |
| CN1240479C (en) * | 2004-05-20 | 2006-02-08 | 沈阳铝镁设计研究院 | Washup-flotation process for stacked bauxite |
| CN101417268A (en) * | 2008-11-26 | 2009-04-29 | 昆明有色冶金设计研究院 | A kind of dressing process for desiliconizing of bauxite |
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2009
- 2009-12-18 CN CN 200910243351 patent/CN101757986B/en active Active
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102205275A (en) * | 2011-05-18 | 2011-10-05 | 昆明理工大学 | Reinforced floatation desilicification method for high-silicon bauxite |
| CN102489411A (en) * | 2011-12-26 | 2012-06-13 | 昆明理工大学 | Flotation two-stage desiliconization method for high-silicon bauxite |
| CN102489411B (en) * | 2011-12-26 | 2013-11-27 | 昆明理工大学 | Flotation two-stage desiliconization method for high-silicon bauxite |
| CN102806146A (en) * | 2012-07-27 | 2012-12-05 | 中国铝业股份有限公司 | Method for performing beneficiation and desilicification on bauxite |
| CN103285625A (en) * | 2013-06-13 | 2013-09-11 | 北京矿冶研究总院 | Defoaming method for reverse flotation desilication of phosphorite |
| CN103285625B (en) * | 2013-06-13 | 2015-08-26 | 北京矿冶研究总院 | Defoaming method for reverse flotation desilication of phosphorite |
| CN103521363B (en) * | 2013-10-19 | 2016-06-22 | 李耀吾 | Low-grade bauxite raw ore open-circuit grinding ore-dressing technique |
| CN103521363A (en) * | 2013-10-19 | 2014-01-22 | 李耀吾 | Low-quality raw bauxite ore open-grinding and dressing technology |
| CN104841567A (en) * | 2015-06-08 | 2015-08-19 | 河南东大矿业股份有限公司 | Flow mixing method for bauxite forward flotation |
| CN107051711A (en) * | 2017-04-10 | 2017-08-18 | 中国铝业股份有限公司 | A kind of method that mineral processing tailing of bauxite is selected again |
| CN107051711B (en) * | 2017-04-10 | 2019-09-13 | 中国铝业股份有限公司 | A kind of method that mineral processing tailing of bauxite selects again |
| CN109158221A (en) * | 2018-08-23 | 2019-01-08 | 广东省大宝山矿业有限公司 | A kind of copper sulphur mine ore-sorting system improving foam pump mounting means |
| CN110876988A (en) * | 2019-12-11 | 2020-03-13 | 太原睿孚特选煤技术有限公司 | Circulation volume automatic compensation pan feeding volume fluctuation's cavitation jet microbubble flotation column |
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