CN107188185A - A kind of utilization quartz sand tailings purifies the production method of high crystobalite sand - Google Patents

A kind of utilization quartz sand tailings purifies the production method of high crystobalite sand Download PDF

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Publication number
CN107188185A
CN107188185A CN201710548875.9A CN201710548875A CN107188185A CN 107188185 A CN107188185 A CN 107188185A CN 201710548875 A CN201710548875 A CN 201710548875A CN 107188185 A CN107188185 A CN 107188185A
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sand
purifies
production method
quartz
stops
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CN201710548875.9A
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璧电ゥ
赵祥
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Linyi Hao Quan Silicon Technology Co Ltd
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Linyi Hao Quan Silicon Technology Co Ltd
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Priority to CN201710548875.9A priority Critical patent/CN107188185A/en
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/113Silicon oxides; Hydrates thereof
    • C01B33/12Silica; Hydrates thereof, e.g. lepidoic silicic acid
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/80Compositional purity

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention discloses the production method that a kind of utilization quartz sand tailings purifies high crystobalite sand, belong to comprehensive utilization of tailing technical field.This method comprises the following steps:1. wash 2. magnetic separation 3. pickling 4. caustic dip 5. drying 6. screen.By above step, quartz tail sand can be processed into the silica flour product for meeting industrial department requirement, the local quartz tail sand of long-standing problem is solved and stack the problem of environmental pollution for taking a large amount of farmlands and thereby resulting in.

Description

A kind of utilization quartz sand tailings purifies the production method of high crystobalite sand
Technical field
The invention belongs to quartz sand production technical field, more particularly to one kind high crystobalite is purified using quartz sand tailings The production method of sand, silicon powder.
Background technology
With the progress of scientific and technological level, many tips such as optical-fibre communications, semiconductor technology, solar cell, science and techniques of defence Field is growing to the demand of high quality quartz sand, and China's high grade quartz sand resource increasingly depleted, it is impossible to meet these necks The demand in domain, improve constantly purification by mineral technology turns into the Main Means for solving the problems, such as glass sand shortage of resources.
In recent years, starting for large quantities of quartzy ore dressing projects is made that product to alleviating active demand of the every profession and trade to siliceous raw material The contribution of pole, while also bringing rich profit to quartz raw material manufacturing enterprise.But thing followed Quartz Tails problem Increasingly highlight, the not only development to enterprise brings no small problem, and huge pollution is also brought to surrounding enviroment, is become The problem of pendulum is in the urgent need to address in face of each quartz raw material manufacturing enterprise.
Shandong Hao Quan silica sands Science and Technology Ltd. produces substantial amounts of tailings while quartz sand is produced, and these tailings are not only Substantial amounts of place storage is taken, the development to enterprise brings no small problem, huge dirt is also brought to surrounding enviroment Dye, becomes the problem of pendulum is in the urgent need to address in face of enterprise.Contrast SiO in washed ore, tailings chemical composition2Content is substantially inclined It is low, while Al2O3、Fe2O3、TiO2It is generally higher Deng impurity component.Tailings quality is not high, and granularity is partially thin, it is necessary to be processed Purification can be used as high-end applications.
Therefore, enterprise puts into the purification research that a large amount of manpower and materials carry out quartz tail sand, target is to obtain SiO2Content height, Fe2O3 containAmount is low, meets the high-end high crystobalite sand product utilized of industry, foundation is provided for the high value added utilization of the mine tailing, and Achieve preferable effect.
The content of the invention
It is an object of the invention to provide a kind of method that utilization quartz sand production waste tailings produces high crystobalite sand.
Quartz tail sand is the thinner crystalloid quartz of granularity, SiO2Content it is general all between 90% to 99%, remaining into Divide with A12O3Based on, exist in the form of mud.In addition, also a small amount of irony, mica etc..Effectively utilize the difficult point of quartz tail sand Mainly wherein aluminium, iron content are higher.The present invention is using washing, magnetic separation, pickling, caustic dip, drying, screening technology, from discarded High crystobalite sand is purified in quartz tail sand, to realize making full use of for resource.
The purpose of the present invention is achieved through the following technical solutions, and this purifies the side of high crystobalite sand using quartz tail sand Method comprises the following steps:
1. wash:Quartz tail sand discharge advance into hydrocyclone desliming, then washed through clear water, be dehydrated after it is standby.
2. magnetic separation:Quartz tail sand by washing desliming is subjected to preliminary iron removal by magnetic separation in magnetic separator.
3. pickling:The tailings added in rotary drum after washing magnetic separation, at normal temperatures, pickling use water 100%, the 0.6-1 % hydrochloric acid is once added, 45 min is rotated, stops 30 min, turn 45min;Second of addition 0.5-1% sulfuric acid, Turn 45 min, stop 30 min, turn 45min, stop 30 min;Third time adds 0.3-0.8% nitric acid, and adds 0.4- 0.7% catalyst sodium formate, turns 45 min, stops 30 min, turn 45min, stop 30 min, stops drum and (stops drum to stay overnight overnight Period, every two hours rotate 5 min), filtering abjection acid solution recycling, with clear water washing material to PH=6-7.
4. caustic dip:In the material after overpickling, sodium hydroxide 1.5-2%, 01.1-0.3% surface-active is first added Agent, rotates 60 min, stops the min of drum 30, adds 0.5% polysorbas20, rotates 60 min, stops 30 min, caustic dip is total 4~6h of time.Filtering abjection recycle of alkali liquor is utilized, subsequently into the program with clear water washing material, i.e. moisturizing, water 30%, 40 min are rotated, continue moisturizing 40%, 30 min are rotated, continue moisturizing 40%, turn 20 min, continue moisturizing 30% ~40%, 20 min are rotated, then be dehydrated standby.
5. dry:In the material feeding drying machine of step 4. after dehydration, dried at a temperature of 200-450 DEG C, Cooling.
6. screen:5. step is screened by drying the material of cooling, the sand of the 70-150 mesh filtered out is finished product, Pack.
It is preferred that, in step 3. pickling procedure, concentration of hydrochloric acid 20%;Liquid-solid ratio:Hydrochloric acid solution:Quartz tail sand is 2:1; Sulfuric acid concentration 25%;Liquid-solid ratio is:Sulfuric acid:Quartz tail sand is 1.5:1.Hydrochloric acid and sulfuric acid solution in technique can be recycled, Recycled after wherein impurities accumulation to finite concentration, it is recycled.
It is preferred that, in step 4. caustic dip process, surfactant is sodium naphthenate, the one or two of pull open powder.
Experiment proves that the leaching molten time of sulfuric acid solution has a significant effect to the removal effect of iron tramp in quartz tail sand, needs Want the enough leaching molten time;But because quartz tail sand particle is thinner, the time is oversize to be possible to deposited phenomenon after producing, and makes going for iron Except effect declines on the contrary, therefore in pickling and caustic dip step, rotation-stopping -- the work that moves in circles of rotation-stopping is selected Skill, while promoting the various auxiliary agents of physical-chemical reaction, such as surfactant, catalyst sodium formate, Ke Yixian by adding The raising acidleach of work and alkali leaching effect,
Proved by strict detection, the technical indicator of the high crystobalite sand produced according to the method described in the present invention is substantially better than The high crystobalite sand of the method production of prior art, technical indicator contrast see the table below.
Product category whiteness(%) Si O2(%) Fe2O3(%)
High crystobalite sand 92.0 99.9 0.008 produced by the invention
The high crystobalite sand 88.3 99.5 0.0 2 of prior art production
It can be drawn, be produced with the high crystobalite sand of method of the present invention production and using prior art by upper table data High crystobalite sand facies ratio, whiteness is significantly increased, Fe2O3Content is significantly reduced, SiO2Increase, reaches 99.9%.Using mechanical force, The fuel factor of the generations such as mechanical friction, impact, the change on the fresh surface of mineral crystal structure, mineral active and chemical composition with And the electrochemical reaction supervened, the more difficult mineral chemically reacted can be enable comparatively easy to carry out, while may be used also So that sour molten, reduction chemical reaction the speed and depth of quartz tail sand is greatly improved, make the leaching rate of the impurity such as institute's iron content at double Improve, the SiO of mineral2Content is significantly improved.
Simultaneously, it is necessary to which it is emphasized that the step such as pickling, caustic dip in method of the present invention is entirely in normal temperature Lower progress, it is not necessary to artificial heating, and the step such as the pickling of prior art, caustic dip is required for temperature being increased to 100 degree of left sides It is right.Therefore method of the present invention compared with prior art, not only increases product quality, also simplify process, reduce Energy consumption.
By the exploitation to quartz tail sand comprehensive utilization technique, quartz tail sand can be processed into and meet industrial department requirement Silica flour product, the environmental pollution for solving the local quartz tail sand a large amount of farmlands of stacking occupancy of long-standing problem and thereby resulting in is asked Topic.
Embodiment
The method for purifying high crystobalite sand using quartz tail sand comprises the following steps:
1. wash:Quartz tail sand discharge advance into hydrocyclone desliming, then washed through clear water, be dehydrated after it is standby.
2. magnetic separation:Quartz tail sand by washing desliming is subjected to preliminary iron removal by magnetic separation in magnetic separator.
3. pickling:The tailings added in rotary drum after washing magnetic separation, at normal temperatures, pickling use water 100%, the Once the % hydrochloric acid of addition 0.8, rotates 45 min, stops 30 min, turn 45min;Second of 0.7% sulfuric acid of addition, turns 45 min, stop 30 min, turn 45min, stop 30 min;Third time adds 0.5% nitric acid, and adds 0.6% catalyst Sodium formate, turns 45 min, stops 30 min, turn 45min, stop 30 min, and stopping drum, (during stopping drum overnight, every two is small overnight When rotate 5 min), filtering abjection acid solution recycling, with clear water washing material to PH=6-7.
4. caustic dip:In the material after overpickling, sodium hydroxide 1% is first added, 0.2% surfactant turns Dynamic 60 min, stop the min of drum 30, add 0.5% polysorbas20, rotate 60 min, stop 30 min, caustic dip total time 4 ~6h.Filtering abjection recycle of alkali liquor is utilized, and subsequently into the program with clear water washing material, i.e. moisturizing, water 30% is rotated 40 min, continue moisturizing 40%, rotate 30 min, continue moisturizing 40%, turn 20 min, and continuation moisturizing 30%~ 40%, 20 min are rotated, then be dehydrated standby.
5. dry:In material feeding drying machine of the step 4 after dehydration, dried at a temperature of 200-450 DEG C, Cooling.
6. screen:Step 5 is screened by drying the material of cooling, the sand of the 60-140 mesh filtered out is finished product, Pack.

Claims (5)

1. a kind of utilization quartz sand tailings purifies the production method of high crystobalite sand, it is characterised in that this method includes following step Suddenly:1. 6. the caustic dip -5. drying-of the pickling of magnetic separation -3. of washing -2. -4. screens.
2. a kind of utilization quartz sand tailings according to claim 1 purifies the production method of high crystobalite sand, its feature exists In 3. pickling:The tailings added in rotary drum after washing magnetic separation, at normal temperatures, pickling use water 100%, add for the first time Enter 0.6-1 % hydrochloric acid, rotate 45 min, stop 30 min, turn 45min;Second of addition 0.5-1% sulfuric acid, turns 45 Min, stops 30 min, turns 45min, stops 30 min;Third time adds 0.3-0.8% nitric acid, and adds urging for 0.4-0.7% Agent sodium formate, turns 45 min, stops 30 min, turn 45min, stop 30 min, stops drum and stays overnight (during stopping drum overnight, often Rotate 5 min within two hours), filtering abjection acid solution recycling, with clear water washing material to PH=6-7.
3. a kind of utilization quartz sand tailings according to claim 1 purifies the production method of high crystobalite sand, its feature exists In 4. caustic dip:In the material after overpickling, sodium hydroxide 1.5-2%, 01.1-0.3% surfactant is first added, 60 min are rotated, stop the min of drum 30,0.5% polysorbas20 is added, 60 min is rotated, stops 30 min, caustic dip total time 4~6h;Filtering abjection recycle of alkali liquor is utilized, and subsequently into the program with clear water washing material, i.e. moisturizing, water 30% is rotated 40 min, continue moisturizing 40%, rotate 30 min, continue moisturizing 40%, turn 20 min, and continuation moisturizing 30%~ 40%, 20 min are rotated, then be dehydrated standby.
4. a kind of utilization quartz sand tailings according to claim 1 or 2 purifies the production method of high crystobalite sand, its feature It is, in step 3. pickling procedure, concentration of hydrochloric acid 20%;Liquid-solid ratio:Hydrochloric acid solution:Quartz tail sand is 2:1;Sulfuric acid concentration 25%;Liquid-solid ratio is:Sulfuric acid:Quartz tail sand is 1.5:1;Hydrochloric acid and sulfuric acid solution in technique can be recycled, when wherein miscellaneous Matter builds up to after finite concentration and recycled, recycled.
5. a kind of utilization quartz sand tailings according to claim 1 or 3 purifies the production method of high crystobalite sand, its feature It is, in step 4. caustic dip process, surfactant is sodium naphthenate, the one or two of pull open powder.
CN201710548875.9A 2017-07-07 2017-07-07 A kind of utilization quartz sand tailings purifies the production method of high crystobalite sand Pending CN107188185A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107501778A (en) * 2017-10-18 2017-12-22 温州市赢创新材料技术有限公司 A kind of low-cost energy-saving construction material and preparation method thereof
CN108640664A (en) * 2018-03-22 2018-10-12 滁州方大矿业发展有限公司 A kind of silica flour for ceramic making
CN111499365A (en) * 2020-04-22 2020-08-07 宜宾学院 Method for whitening weathered sandstone through acid-base combined treatment
CN115246647A (en) * 2022-07-28 2022-10-28 苏州清控环保科技有限公司 Quartz sand iron remover and treatment method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103372496A (en) * 2013-06-21 2013-10-30 田辉明 Process method for separating quartz sand, arkosic sand and iron powder from river yellow sand
CN103613102A (en) * 2013-12-04 2014-03-05 南京工业大学东海先进硅基材料研究院 Process for preparing ultrahigh pure quartz sand through silica raw material
CN103880278A (en) * 2014-02-25 2014-06-25 连云港市弘扬石英制品有限公司 Preparation method of optical fiber covering quartz capillary perform and continuous melting furnace equipment
CN103964444A (en) * 2014-05-05 2014-08-06 临沂晟泉矿业有限公司 Method for producing high-purity quartz sand
CN103979546A (en) * 2014-05-05 2014-08-13 临沂晟泉矿业有限公司 Method for producing purified high-whiteness quartz sand and silica micropowder from quartz sand tailings

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103372496A (en) * 2013-06-21 2013-10-30 田辉明 Process method for separating quartz sand, arkosic sand and iron powder from river yellow sand
CN103613102A (en) * 2013-12-04 2014-03-05 南京工业大学东海先进硅基材料研究院 Process for preparing ultrahigh pure quartz sand through silica raw material
CN103880278A (en) * 2014-02-25 2014-06-25 连云港市弘扬石英制品有限公司 Preparation method of optical fiber covering quartz capillary perform and continuous melting furnace equipment
CN103964444A (en) * 2014-05-05 2014-08-06 临沂晟泉矿业有限公司 Method for producing high-purity quartz sand
CN103979546A (en) * 2014-05-05 2014-08-13 临沂晟泉矿业有限公司 Method for producing purified high-whiteness quartz sand and silica micropowder from quartz sand tailings

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107501778A (en) * 2017-10-18 2017-12-22 温州市赢创新材料技术有限公司 A kind of low-cost energy-saving construction material and preparation method thereof
CN108640664A (en) * 2018-03-22 2018-10-12 滁州方大矿业发展有限公司 A kind of silica flour for ceramic making
CN111499365A (en) * 2020-04-22 2020-08-07 宜宾学院 Method for whitening weathered sandstone through acid-base combined treatment
CN111499365B (en) * 2020-04-22 2022-05-20 宜宾学院 Method for whitening weathered sandstone through acid-base combined treatment
CN115246647A (en) * 2022-07-28 2022-10-28 苏州清控环保科技有限公司 Quartz sand iron remover and treatment method thereof

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