CN101028610A - Iron-removing concentrating process of potash feldspar - Google Patents
Iron-removing concentrating process of potash feldspar Download PDFInfo
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- CN101028610A CN101028610A CNA2007100616704A CN200710061670A CN101028610A CN 101028610 A CN101028610 A CN 101028610A CN A2007100616704 A CNA2007100616704 A CN A2007100616704A CN 200710061670 A CN200710061670 A CN 200710061670A CN 101028610 A CN101028610 A CN 101028610A
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Abstract
An iron-removing ore dressing technology for potash feldspar includes such steps as washing, breaking, sorting, concentrating, purifying, washing with sulfuric acid and sieving. It has high output (more than 90%), low content of Fe (less than 0.24%) and more by-products (silt, Fe, mica, Fe2O3 and Fe3O4).
Description
Technical field
The present invention relates to a kind of ore-dressing technique, specifically a kind of iron-removing concentrating process of potassic feldspar.
Background technology
The beneficiation method that is used at present potash feldspar deferrization both at home and abroad mainly is magnetic separation and flotation.As Geju City, Yunnan potash feldspar ore, he adopts the choosing of dry powder magnetic force, although its easy processing, its technological process is aging, and is outmoded, the processing cost height, power consumption is big, and profit is few, and usefulness is low, the product dullness, byproduct can not fully utilize, and one meets wind slightly, stirs up a cloud of dust, and air pollution is serious.The Hubei potash feldspar ore adopts flotation, and its weak point is, need add chemical substance, the production cost height, and serious waste of resources, environmental protection efficacy is poor.
Summary of the invention
Goal of the invention of the present invention is exactly at the above-mentioned defective that exists in the prior art, provides a kind of technology simple science, and production cost is low, and sealing is produced free from environmental pollution, produces the iron-removing concentrating process of the high potassic feldspar of multiple byproduct comprehensive utilization ratio.
Realize the foregoing invention purpose by the following technical solutions: a kind of iron-removing concentrating process of potassic feldspar, it comprises: with the potassic feldspar crusher in crushing, broken material is sent into the rotary screen screening, granularity is that the particle below 6 millimeters is sent into grinding machine and ground to form 20-200 purpose fine powder, also comprise following processing step
A, wash mud: 20-200 purpose powder material is sent into spiral chute, separate sorting, select silt;
B, sorting: the material that will remove silt after sorting is sent into shaking table, washes out di-iron trioxide;
C, selected: the material that will remove di-iron trioxide is sent into the strong magnetic gravity concentrator of 1024 types and is carried out selectedly, selects iron, mica material, then material is sent into the general magnetic separator of 1018 * 2 types, selects iron, mica material once more;
D, purification: will send into the high frequency shale shaker screening through the material of gravity treatment and general election, and reject di-iron trioxide and tri-iron tetroxide in the material powder, and obtain the potassic feldspar fine powder;
E, the smart powder of pickling: use sulfuric acid as mordant, blend according to the concentration of sulfuric acid and the iron-holder of potassic feldspar fine powder, under the situation that sulfuric acid concentration is determined, the iron-holder of potassic feldspar fine powder is directly proportional with the sulfuric acid weight that is added, thoroughly remove di-iron trioxide and tri-iron tetroxide through pickling, isolate copperas solution, obtain the smart powder of potassic feldspar;
F, the smart powder of screening potassic feldspar: the smart powder of potassic feldspar is sent into the screening of 20-200 mesh sieve, and screenings is that iron content is lower than 0.24% finished product.
According to technique scheme, compared with prior art, to smart powder, the rate of recovery reaches more than 90% from raw ore in the present invention; Its technological process is simple, and is easy to operate.The byproduct kind of production and processing in this technology is many, all is the primary raw material that industry needs, and the resource utilization height reaches the purpose of comprehensive utilization.It is also advantageous in that significantly whole technology is not provided with the silt storehouse, and minimizing occupies cultivated land, closed circulation production, the problem that does not stir up a cloud of dust; Industrial water recycles, the amount of conserving water, protection environmental resource.
The specific embodiment
The invention is further illustrated by the following examples:
Potassic feldspar adopts Qianxi County, Hebei province and the domestic potassic feldspar of Zunhua County, and essential mineral content (weight) is: potassic feldspar is more than 90%, annite 2%, iron 5%, kaolin 2%.
Concrete processing step is as follows:
By ore dressing routine operation method with potassic feldspar with 500 * 700 crusher in crushing, it is broken once more that broken material is sent into 135 hammer-crushers, particle after the fragmentation is sent into 1.2 * 3.6 meters rotary screen screening, the undersize degree is that the particle below 6 millimeters is sent into 1.83 * 7 meters grinding machine and ground to form 20-200 purpose fine powder, and its fineness is selected according to customer requirements.
Also comprise following processing step,
Wash mud: 20-200 purpose material is sent into 1.2 * 4 * 40 spiral chute, and material per ton adds 6 tons of water and separates sorting, selects byproduct silt (kaolin);
Sorting: the material that will select behind the silt is sent into 2.5 * 6 * 25 meters shaking table, washes out Fe
2O
3
Selected: as will to wash out Fe through shaking table
2O
3Material send into the strong magnetic gravity concentrator of 1024 types and carry out selected, material is that to carry out wet high-intensity magnetic under the field intensity of 8000-10000 selected in magnetic field intensity, select byproduct iron, mica material, then material is sent into the general magnetic separator of 1018 * 2 types, be that to carry out magnetic under the field intensity of 1200-1600 selected in magnetic field intensity, select iron, mica material once more;
Purify: will send into 2.4 * 3.2 * 4 meters high frequency shale shaker screening through the material of gravity treatment and general election, screenings is the potassic feldspar fine powder, and oversize is byproduct Fe
2O
3And Fe
3O
4
The smart powder of pickling: use sulfuric acid as mordant, blend according to the concentration of sulfuric acid and the iron-holder of potassic feldspar powder material, the addition of sulfuric acid (weight) is directly proportional with the iron-holder (weight) of material, generally speaking, selecting concentration for use is the sulfuric acid of 10-60%, as: 3 tons of 100 tons of potassic feldspar powder material iron content, need to add 3 tons of sulfuric acid and carry out pickling, thoroughly remove di-iron trioxide and tri-iron tetroxide, isolate copperas solution, obtain the smart powder of potassic feldspar;
Sieve smart powder: the smart powder of potassic feldspar is sent into the screening of 20-200 mesh sieve, and screenings is that iron content is lower than 0.24% 20-200 purpose finished product K
2The O elaboration, this product precision is higher than national standard (0.3), is the primary raw material of glass, ceramic field.
Whole byproducts that whole technology of the present invention is selected from start to end all are industrial materials, do not have waste material.
Claims (1)
1, a kind of iron-removing concentrating process of potassic feldspar, it comprises: with the potassic feldspar crusher in crushing, broken material is sent into the rotary screen screening, and granularity is that the particle below 6 millimeters is sent into grinding machine and ground to form fine powder, it is characterized in that, also comprises following processing step,
A, wash mud: 20-200 purpose powder material is sent into spiral chute, separate sorting, select silt;
B, sorting: the material that will remove silt after sorting is sent into shaking table, washes out di-iron trioxide;
C, selected: the material that will remove di-iron trioxide is sent into the strong magnetic gravity concentrator of 1024 types and is carried out selectedly, selects iron, mica material, then material is sent into the general magnetic separator of 1018 * 2 types, selects iron, mica material once more;
D, purification: will send into the high frequency shale shaker screening through the material of gravity treatment and general election, and reject di-iron trioxide and tri-iron tetroxide in the material powder, and obtain the potassic feldspar fine powder;
E, the smart powder of pickling: use sulfuric acid as mordant, blend according to the concentration of acid and the iron-holder of potassic feldspar fine powder, under the situation that sulfuric acid concentration is determined, the iron-holder of potassic feldspar fine powder is directly proportional with the sulfuric acid weight that is added, thoroughly remove di-iron trioxide and tri-iron tetroxide through pickling, isolate copperas solution, obtain the smart powder of potassic feldspar;
F, the smart powder of screening potassic feldspar: the smart powder of potassic feldspar is sent into the screening of 20-200 mesh sieve, and screenings is that iron content is lower than 0.24% finished product.
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CNB2007100616704A CN100569381C (en) | 2007-04-06 | 2007-04-06 | The iron-removing concentrating process of potassic feldspar |
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CNB2007100616704A CN100569381C (en) | 2007-04-06 | 2007-04-06 | The iron-removing concentrating process of potassic feldspar |
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CN100569381C CN100569381C (en) | 2009-12-16 |
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Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101623670B (en) * | 2009-07-27 | 2011-08-17 | 山东科力华电磁设备有限公司 | Technique for extracting iron ore concentrate powder from sand iron mine of gobi desert |
CN102284352A (en) * | 2011-08-08 | 2011-12-21 | 中南大学 | Efficient ore dressing and impurity removal process for potassium and sodium feldspar ores which are complex and difficult to process and combined medicament thereof |
CN102441496A (en) * | 2011-10-14 | 2012-05-09 | 中科翔(天津)科技有限公司 | Method for selecting potassium feldspars in potassium-bearing tailings |
CN102631979A (en) * | 2012-04-18 | 2012-08-15 | 赣州金环磁选设备有限公司 | Magnetic ore dressing method of high-quality feldspar ore |
CN103449531A (en) * | 2013-08-19 | 2013-12-18 | 铜陵瑞莱科技有限公司 | Preparation method of iron oxide red for artificial marbles |
CN103752401A (en) * | 2013-12-28 | 2014-04-30 | 中国地质科学院郑州矿产综合利用研究所 | Potash feldspar iron removal process |
CN104925823A (en) * | 2015-06-08 | 2015-09-23 | 田晋丞 | Process for refining hematite type potassium feldspar sand powder |
CN105344473A (en) * | 2015-10-29 | 2016-02-24 | 许树清 | Method for processing coal mine roof aluminum shale to separate kaolin |
CN105921258A (en) * | 2016-04-29 | 2016-09-07 | 洛南县大秦钾矿有限公司 | Method for impurity removal and whitening of potassium feldspar |
CN106040419A (en) * | 2016-06-14 | 2016-10-26 | 蚌埠玻璃工业设计研究院 | Purifying and whitening method for weathered feldspar |
CN108057513A (en) * | 2017-12-20 | 2018-05-22 | 江西九岭新能源有限公司 | The method that the barren rock of giant granite containing lithium extracts potassium feldspar concentrate and zinnwaldite concentrate |
CN108863071A (en) * | 2018-08-30 | 2018-11-23 | 贺州市骏鑫矿产品有限责任公司 | A kind of glaze feldspar in powder and preparation method thereof |
CN108976846A (en) * | 2018-09-30 | 2018-12-11 | 江门市精达云母材料有限公司 | A kind of processing technology of mica powder |
CN109107751A (en) * | 2018-08-31 | 2019-01-01 | 贺州市骏鑫矿产品有限责任公司 | A kind of flotation impurity removal process from low grade potassium albite ore |
CN109261349A (en) * | 2018-08-31 | 2019-01-25 | 贺州市骏鑫矿产品有限责任公司 | A kind of purification method of whitening of albite |
CN109569872A (en) * | 2018-11-21 | 2019-04-05 | 衡阳县天宇陶瓷矿业有限公司 | A kind of method and its feldspar fine powder being classified using hydrometer method to feldspar iron-removing |
CN109622210A (en) * | 2018-12-27 | 2019-04-16 | 中建材蚌埠玻璃工业设计研究院有限公司 | A kind of method of weathering type potash feldspar ore gradation grade purification |
CN110898955A (en) * | 2019-11-06 | 2020-03-24 | 乐山市南联环资科技有限责任公司 | Process for producing feed additive by using feldspar tailings |
-
2007
- 2007-04-06 CN CNB2007100616704A patent/CN100569381C/en not_active Expired - Fee Related
Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101623670B (en) * | 2009-07-27 | 2011-08-17 | 山东科力华电磁设备有限公司 | Technique for extracting iron ore concentrate powder from sand iron mine of gobi desert |
CN102284352A (en) * | 2011-08-08 | 2011-12-21 | 中南大学 | Efficient ore dressing and impurity removal process for potassium and sodium feldspar ores which are complex and difficult to process and combined medicament thereof |
CN102284352B (en) * | 2011-08-08 | 2013-05-08 | 中南大学 | Efficient ore dressing and impurity removal process for potassium and sodium feldspar ores which are complex and difficult to process and combined medicament thereof |
CN102441496A (en) * | 2011-10-14 | 2012-05-09 | 中科翔(天津)科技有限公司 | Method for selecting potassium feldspars in potassium-bearing tailings |
CN102441496B (en) * | 2011-10-14 | 2013-07-10 | 中科翔(天津)科技有限公司 | Method for selecting potassium feldspars in potassium-bearing tailings |
CN102631979A (en) * | 2012-04-18 | 2012-08-15 | 赣州金环磁选设备有限公司 | Magnetic ore dressing method of high-quality feldspar ore |
CN103449531A (en) * | 2013-08-19 | 2013-12-18 | 铜陵瑞莱科技有限公司 | Preparation method of iron oxide red for artificial marbles |
CN103449531B (en) * | 2013-08-19 | 2016-03-09 | 铜陵瑞莱科技有限公司 | A kind of preparation method of artificial marble red iron oxide |
CN103752401A (en) * | 2013-12-28 | 2014-04-30 | 中国地质科学院郑州矿产综合利用研究所 | Potash feldspar iron removal process |
CN103752401B (en) * | 2013-12-28 | 2015-12-02 | 中国地质科学院郑州矿产综合利用研究所 | Potash feldspar iron removal process |
CN104925823A (en) * | 2015-06-08 | 2015-09-23 | 田晋丞 | Process for refining hematite type potassium feldspar sand powder |
CN105344473A (en) * | 2015-10-29 | 2016-02-24 | 许树清 | Method for processing coal mine roof aluminum shale to separate kaolin |
CN105921258A (en) * | 2016-04-29 | 2016-09-07 | 洛南县大秦钾矿有限公司 | Method for impurity removal and whitening of potassium feldspar |
CN106040419A (en) * | 2016-06-14 | 2016-10-26 | 蚌埠玻璃工业设计研究院 | Purifying and whitening method for weathered feldspar |
CN108057513A (en) * | 2017-12-20 | 2018-05-22 | 江西九岭新能源有限公司 | The method that the barren rock of giant granite containing lithium extracts potassium feldspar concentrate and zinnwaldite concentrate |
CN108863071A (en) * | 2018-08-30 | 2018-11-23 | 贺州市骏鑫矿产品有限责任公司 | A kind of glaze feldspar in powder and preparation method thereof |
CN108863071B (en) * | 2018-08-30 | 2021-04-20 | 贺州市骏鑫矿产品有限责任公司 | Potassium feldspar powder for glaze and preparation method thereof |
CN109107751A (en) * | 2018-08-31 | 2019-01-01 | 贺州市骏鑫矿产品有限责任公司 | A kind of flotation impurity removal process from low grade potassium albite ore |
CN109261349A (en) * | 2018-08-31 | 2019-01-25 | 贺州市骏鑫矿产品有限责任公司 | A kind of purification method of whitening of albite |
CN109107751B (en) * | 2018-08-31 | 2021-04-20 | 贺州市骏鑫矿产品有限责任公司 | Flotation impurity removal process for low-grade potassium-sodium feldspar ore |
CN108976846A (en) * | 2018-09-30 | 2018-12-11 | 江门市精达云母材料有限公司 | A kind of processing technology of mica powder |
CN109569872A (en) * | 2018-11-21 | 2019-04-05 | 衡阳县天宇陶瓷矿业有限公司 | A kind of method and its feldspar fine powder being classified using hydrometer method to feldspar iron-removing |
CN109622210A (en) * | 2018-12-27 | 2019-04-16 | 中建材蚌埠玻璃工业设计研究院有限公司 | A kind of method of weathering type potash feldspar ore gradation grade purification |
CN110898955A (en) * | 2019-11-06 | 2020-03-24 | 乐山市南联环资科技有限责任公司 | Process for producing feed additive by using feldspar tailings |
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