CN100569381C - The iron-removing concentrating process of potassic feldspar - Google Patents

The iron-removing concentrating process of potassic feldspar Download PDF

Info

Publication number
CN100569381C
CN100569381C CNB2007100616704A CN200710061670A CN100569381C CN 100569381 C CN100569381 C CN 100569381C CN B2007100616704 A CNB2007100616704 A CN B2007100616704A CN 200710061670 A CN200710061670 A CN 200710061670A CN 100569381 C CN100569381 C CN 100569381C
Authority
CN
China
Prior art keywords
iron
potassic feldspar
sent
powder
smart powder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CNB2007100616704A
Other languages
Chinese (zh)
Other versions
CN101028610A (en
Inventor
王连民
王轶新
赵春德
吴雨川
林秀莲
林青莲
孙翠华
刘恩水
李晓玲
唐利智
Original Assignee
王连民
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 王连民 filed Critical 王连民
Priority to CNB2007100616704A priority Critical patent/CN100569381C/en
Publication of CN101028610A publication Critical patent/CN101028610A/en
Application granted granted Critical
Publication of CN100569381C publication Critical patent/CN100569381C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

A kind of iron-removing concentrating process of potassic feldspar belongs to ore-dressing technique.It comprises conventional crushing process and sieving technology, also comprise and wash mud, sorting, selected, purify, with the smart powder of sulfuric acid washing, the smart powder craft of screening potassium, sub-elect silt, iron, mica material according to processing step, byproducts such as di-iron trioxide and tri-iron tetroxide obtain iron content at last and are lower than 0.24% finished product.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, the resource utilization height.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.

Description

The iron-removing concentrating process of potassic feldspar
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 1.2 * 4 * 40 meters spiral chute, separate sorting, select silt;
B, sorting: the material that will remove silt after sorting is sent into 2.5 * 6 * 25 meters 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.
CNB2007100616704A 2007-04-06 2007-04-06 The iron-removing concentrating process of potassic feldspar Expired - Fee Related CN100569381C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2007100616704A CN100569381C (en) 2007-04-06 2007-04-06 The iron-removing concentrating process of potassic feldspar

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2007100616704A CN100569381C (en) 2007-04-06 2007-04-06 The iron-removing concentrating process of potassic feldspar

Publications (2)

Publication Number Publication Date
CN101028610A CN101028610A (en) 2007-09-05
CN100569381C true CN100569381C (en) 2009-12-16

Family

ID=38714269

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2007100616704A Expired - Fee Related CN100569381C (en) 2007-04-06 2007-04-06 The iron-removing concentrating process of potassic feldspar

Country Status (1)

Country Link
CN (1) CN100569381C (en)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
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
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
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
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
CN104925823B (en) * 2015-06-08 2017-09-29 黄冈师范学院 A kind of purifying technique of hematite-type potassium feldspar emery dust
CN105344473B (en) * 2015-10-29 2017-07-04 许树清 The coal mine roof plate aluminium shale processing kaolinic method of sorting
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
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
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
CN109261349B (en) * 2018-08-31 2020-05-19 贺州市骏鑫矿产品有限责任公司 Method for purifying and whitening albite
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
CN109622210B (en) * 2018-12-27 2021-02-05 中建材蚌埠玻璃工业设计研究院有限公司 Method for purifying weathered potash feldspar ore in grading grade
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

Also Published As

Publication number Publication date
CN101028610A (en) 2007-09-05

Similar Documents

Publication Publication Date Title
CN100569381C (en) The iron-removing concentrating process of potassic feldspar
CN103752401B (en) Potash feldspar iron removal process
CN100592933C (en) Novel rhombohedral iron ore beneficiation technics
CN109894257B (en) Comprehensive utilization method for spodumene beneficiation
CN101502819B (en) Pre-selection method of low-ore grade magnetic iron ore
CN102500465B (en) Benefication method for bastnaesite
CN101537394B (en) Chemical-adding scrubbing beneficiation and enrichment method suitable for clay vanadium ore
CN105921258A (en) Method for impurity removal and whitening of potassium feldspar
CN102189037A (en) Impurity removal process for quartz sand
CN110743685B (en) Method for preparing superfine high-whiteness micro powder by removing impurities from granite fine particle powder in full size fraction
CN110328047B (en) Method for preparing ceramic raw material from granite stone sawn mud stone powder
CN105478232B (en) A kind of beneficiation method from graphite mould navajoite enrichment vanadic anhydride
CN102631979A (en) Magnetic ore dressing method of high-quality feldspar ore
CN106583051B (en) Method for full-sludge flotation co-enrichment recovery of lithium niobium tantalum multi-metal resources
CN108380379A (en) A kind of low-grade magnetic mirror iron ore efficient and environment-friendly type beneficiation method
CN105032598A (en) Method for floatation of preconcentration vanadium from high-calcium mica type vanadium-bearing stone coal
CN105903562A (en) Method for extracting iron ore concentrate from flyash
CN107149978A (en) A kind of ore-dressing technique that tumbling ball mill is substituted with agitating mill
CN108993760A (en) A kind of low-grade difficulty of weathering selects manganese ore sorting process
CN108940576B (en) Low-cost potassium-sodalite production method
CN108031546A (en) A kind of method of red mud recycling iron
CN104138793A (en) Reselection impurity removal method for talcum ore containing ferrous sulfide
CN114405659A (en) Process method for producing ceramic material based on granite machine-made sand tailings
CN103386375B (en) A kind of screening technique of molybdenum concntrate
CN111375485B (en) Phosphate ore washing and grading separation method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20091216

Termination date: 20120406