CN107235502A - The method that calcirm-fluoride finished product is prepared using calcium fluoride containing sludge - Google Patents

The method that calcirm-fluoride finished product is prepared using calcium fluoride containing sludge Download PDF

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Publication number
CN107235502A
CN107235502A CN201710678875.0A CN201710678875A CN107235502A CN 107235502 A CN107235502 A CN 107235502A CN 201710678875 A CN201710678875 A CN 201710678875A CN 107235502 A CN107235502 A CN 107235502A
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fluoride
calcium fluoride
auxiliary agent
calcirm
containing sludge
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CN201710678875.0A
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CN107235502B (en
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应盛荣
闻涛
姜战
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Dingsheng Chemical & Technology Co Ltd
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Dingsheng Chemical & Technology Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/20Halides
    • C01F11/22Fluorides
    • 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
    • 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
    • C01P2006/82Compositional purity water content

Abstract

The present invention proposes a kind of method that utilization calcium fluoride containing sludge prepares calcirm-fluoride finished product, including:Mix calcium fluoride containing sludge and auxiliary agent A;The auxiliary agent A removes silica with the silicon dioxde reaction in the calcium fluoride containing sludge, is filtrated to get solution and sediment;The auxiliary agent A is for alkali lye or/and containing alkali waste water;The sediment and auxiliary agent B are mixed, the auxiliary agent B turns into calcirm-fluoride with the calcium hydroxide reaction in the sediment;Reacted with other hydroxide, become solution, removed;Calcium fluoride precipitate is obtained after cleaning, filtering produces calcirm-fluoride finished product.The operating procedure of the present invention is simple, and is that continuous circulation is carried out, and is easy to industrial application.In the obtained calcirm-fluoride finished product of the present invention, Calcium Fluoride Content is 95.0%~99.9%, belongs to high-grade artificial Fluorspar Powder, has a wide range of application.

Description

The method that calcirm-fluoride finished product is prepared using calcium fluoride containing sludge
Technical field
The present invention relates to calcium fluoride sludge processing technology field, particularly relate to a kind of prepared using calcium fluoride containing sludge and be fluorinated The method of calcium finished product.
Background technology
Calcirm-fluoride is the main original for preparing fluorochemical such as hydrofluoric acid, cryolith, aluminum fluoride on chemical industry Material, in addition, fluorite fusing point is low, is widely used in the industry such as metallurgy, cement, glass, ceramics;Transparent colourless or colored firefly Stone can also be used to prepare optical lens and handicraft.
Calcirm-fluoride (fluorite) belongs to non-renewable resources, and fluorite ore resource consumption is too fast, it is accordingly required in particular to protect.From 1999 Nian Qi, China is protected fluorite as strategic resource.The recycling for carrying out fluorine resource is the preferably square of protection fluorine resource Method.
It was found from fluorine product is using process, the industry production such as electronics, glass corrosion, photovoltaic, LED illumination, plating, electrolytic aluminium Fluoride waste can be all produced after the fluorine-containing product use that line is added, and eventually becomes calcium fluoride sludge.These industries are consumed every year Various hydrofluoric acid and fluorine-containing product, the total amount for being converted into 100%HF is expected to be 33.5 ten thousand tons;When the absorptivity absorbed with water is When 90%, the total fluoro quantity in waste water is up to 30.2 ten thousand tons.Calcium fluoride sludge (butt) 62 will be produced during wastewater treatment qualified discharge Ten thousand tons;The moisture content of actual calcium fluoride sludge is about 103~1,240,000 tons for the annual production of 40~50%, i.e. calcium fluoride sludge.
At present, it is allowed to calcium fluoride sludge conventional treatment method have 4 kinds:Fill, burn common brick, mud of heating up water, resource comprehensive profit With.
Landfill:Refer to qualified company, in specified place, after being solidified according to the program of regulation, make landfill stabilization. Advantage is simple, conveniently.Have the disadvantage the higher wasting of resources, cost of disposal, land occupation, possible polluted underground water.
Burn common brick:Refer to qualified common brick factory, be mixed into using calcium fluoride sludge as raw material in clay, fired as common brick. Advantage be it is simple, conveniently, utilization of resources.Have the disadvantage that consumption is few, can not consume comprehensively;And various regions are all in limitation common brick Factory.
Heat up water mud:Refer to qualified cement plant, be mixed into using calcium fluoride sludge as raw material in cement raw material, instead of part Calcium fluoride raw material, is fired as cement.Advantage be it is simple, conveniently, utilization of resources.Have the disadvantage that adaptability is narrow, be not each water Mud factory can use, and consumption is few, can not consume comprehensively.
Current comprehensive utilization of resources includes:(need to dry, add high-quality Fluorspar Powder, granulation etc.) for steel and iron manufacturing. Applied to concrete manufacture (but possible fluorine leaching content can be exceeded).CaF2 in flotation fluorine-containing sludge is mixed into high-quality Fluorspar Powder (flotation difficulty is larger, cost is high, content is low, still have mud discharging).As the raw material of ceramic post sintering, (mixed volume is few, in sludge Impurity content influence ceramic mass).In these modes, the fluorination manufactured except steel industry in part using calcium fluoride sludge Outside calcisphere grain, the practical application of other manner is simultaneously few.
In CN106936386A, a kind of preparation method of artificial Fluorite pellet is disclosed, the calcirm-fluoride that it is obtained is because of content It is low, be only limitted to smelting iron and steel and use, and to be mixed into greater number of technical grade Fluorspar Powder, the economic value of comprehensive utilization compared with It is low.
In CN105905933A, fluoride waste with calcium hydroxide precipitation be calcium fluoride sludge (Calcium Fluoride Content 65%~ 70%), while low concentration fluoride waste and calcium chloride reaction generation calcirm-fluoride and by crystalline silica nuclei in fluidized bed Middle crystallization is calcium fluoride crystal (Calcium Fluoride Content 90%~95%), then calcium fluoride sludge, calcium fluoride crystal and binding agent are mixed Granulating and forming after conjunction, as fluorite finished product.The technology is a kind of method of fluorine containing waste water processing, is can not be calcium fluoride sludge In the case of purification, the form being mixed with using high level calcium fluoride crystal improves the effective content of calcium fluoride sludge;It is led Want problem to crystallize out calcium fluoride crystal in low concentration fluoride waste, fluidized bed huge structure certainly will be caused, investment is very high; Also, low production efficiency, the grade of final finished fluorite (calcirm-fluoride) is low.
Method operating cost height, the treatment effeciency of existing processing calcium fluoride sludge are low, the calcium fluoride sludge warp after processing Ji is worth low, fluorine serious waste of resources.
The content of the invention
The present invention proposes a kind of method that utilization calcium fluoride containing sludge prepares calcirm-fluoride finished product, and solution is run in the prior art Costly, treatment effeciency is low, economic value is low, fluorine serious waste of resources the problems such as.
The technical proposal of the invention is realized in this way:
A kind of method that utilization calcium fluoride containing sludge prepares calcirm-fluoride finished product, including:
Mix calcium fluoride containing sludge and auxiliary agent A;The auxiliary agent A is gone with the silicon dioxde reaction in the calcium fluoride containing sludge Except silica, solution and sediment are filtrated to get;The auxiliary agent A is for alkali lye or/and containing alkali waste water;
The sediment and auxiliary agent B are mixed, the auxiliary agent B turns into fluorination with the calcium hydroxide reaction in the sediment Calcium;Reacted with other hydroxide, become solution, removed;Calcium fluoride precipitate is obtained after cleaning, filtering produces fluorination Calcium finished product;The auxiliary agent B is hydrofluoric acid or/and the waste water of hydrofluoric acid containing;
The calcirm-fluoride finished product, its Calcium Fluoride Content is 95.0%~99.9%.
As preferred technical scheme, the auxiliary agent A and the reaction temperature of the silica in the calcium fluoride containing sludge For normal temperature~150 DEG C.
As preferred technical scheme, the auxiliary agent A obtains water with the silicon dioxde reaction in the calcium fluoride containing sludge Glass.Waterglass finished product can be used as after separation.
As preferred technical scheme, the auxiliary agent A and the product of the aluminium hydroxide reaction in the calcium fluoride containing sludge For sodium aluminate solution.
As preferred technical scheme, the reaction temperature of the auxiliary agent B and the hydroxide in the sediment is normal temperature ~95 DEG C.
As preferred technical scheme, the calcium fluoride containing sludge is after the neutralization reaction of fluoride waste calcium hydroxide is handled Sediment;CaF2 contents are 50~80%wt in the calcium fluoride sludge, and SiO2 contents are 1~30%wt, CaO (including Ca (OH) 2 and CaCO3) content be 2~35%wt, the contents of Al (OH) 3 be 0~20%wt, surplus be other hydroxide.
By auxiliary agent A and auxiliary agent B, most of impurity in calcium fluoride sludge is removed, high-grade calcirm-fluoride is being obtained While finished product, waterglass and water purification agent byproduct are also obtained;Moreover, auxiliary agent A and auxiliary agent B can be the useless of other industries Thing;It is truly realized twice laid, each doing his best.
Beneficial effect
(1) operating procedure of the invention is simple, and is that continuous circulation is carried out, and is easy to industrial application.
(2) in obtained calcirm-fluoride finished product of the invention, Calcium Fluoride Content is 95.00%~99.99%, belongs to high-grade Artificial Fluorspar Powder, has a wide range of application.
(3) by calcium fluoride containing sludge being extracted as the realization of calcirm-fluoride finished product technology, calcirm-fluoride finished product is processed as fluorination Hydrogen (hydrofluoric acid) and villiaumite are possibly realized.By taking electronics industry as an example:Due to using hydrofluoric acid, substantial amounts of calcirm-fluoride is generated dirty Mud, landfill disposal cost is high, pollution environment, land occupation;, can be again using the technology and associated subsequent technology The hydrofluoric acid needed for production is made in calcium fluoride sludge, the recycling economy circle of a complete fluorinated product is formed.
(4) a number of hydrofluoric acid containing waste water can be consumed in preparation process of the invention, makes fluoride wastewater treatment cost Decline.
(5) it can consume a number of containing alkali waste water in preparation process of the invention, and be converted into waterglass finished product, become useless For treasured.
Embodiment
The technical scheme in the embodiment of the present invention will be clearly and completely described below, it is clear that described implementation Example only a part of embodiment of the invention, rather than whole embodiments.Based on the embodiment in the present invention, this area is common The every other embodiment that technical staff is obtained under the premise of creative work is not made, belongs to the model that the present invention is protected Enclose.
Only contain micro aluminium ion, barium ions, strontium ion and magnesium ion in calcium fluoride sludge in following embodiments; In other embodiments, if containing more barium ions, strontium ion and magnesium ion etc.;Can also by with auxiliary agent A or auxiliary agent B Reaction and remove.
High-grade fluorite is only obtained by adding alkali and the step of acid adding two in following embodiments, reactions steps are few, flow It is short, save power consumption.Certain waste water can also be consumed simultaneously, reach turn waste into wealth, the purpose of Environment control, be suitable for extensive Popularization and application.
Embodiment 1
The material used in the embodiment is:Calcium fluoride sludge 1667kg (moisture content 40%) after fluoride wastewater treatment; Butt component:CaF2 contents are 65%wt, and SiO2 contents are 18%wt, and the contents of Ca (OH) 2 are 9%wt, other impurity 7%wt.
A kind of method that utilization calcium fluoride containing sludge prepares calcirm-fluoride finished product, comprises the following steps:
In 10M330% liquid caustic soda 800kg is added in stirred autoclave A;Stirring is opened, calcium fluoride sludge 1667kg is added;Directly Connect into steam heating, reaction temperature is controlled at 75 DEG C, after reacting 2 hours, material is pumped into plate and frame filter press, filtered out Solution is waterglass;Filter cake is pushed into stirred autoclave B, stirring adds 40% hydrofluoric acid 63kg after 20 minutes;Continue to react 10 minutes, whole materials are pumped into plate and frame filter press, the filtrate feeding Sewage Disposal filtered out, it is fluorination to obtain filter cake Calcium product 1202kg, moisture content 38%, Calcium Fluoride Content 99.2%.
Embodiment 2
The material used in the embodiment is:Calcium fluoride sludge 1667kg (moisture content 40%) after fluoride wastewater treatment; Butt component:CaF2 contents are 65%wt, and SiO2 contents are 18%wt, and the contents of Ca (OH) 2 are 9%wt, other impurity 7%wt.
A kind of method that utilization calcium fluoride containing sludge prepares calcirm-fluoride finished product, comprises the following steps:
In 10M330% liquid caustic soda 800kg is added in stirred autoclave A;Stirring is opened, calcium fluoride sludge 1667kg is added;Directly Connect into boiling is steam heated to, after reacting 30 minutes, material is pumped into plate and frame filter press, the solution filtered out is water glass Glass;Filter cake is pushed into stirred autoclave B, stirring adds the waste water 835kg of hydrofluoric acid containing concentration 3% after 20 minutes;Continue to react 20 minutes, whole materials are pumped into plate and frame filter press, the filtrate feeding Sewage Disposal filtered out, it is fluorination to obtain filter cake Calcium product 1207kg, moisture content 38%, Calcium Fluoride Content 99.6%.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all essences in the present invention God is with principle, and any modification, equivalent substitution and improvements made etc. should be included in the scope of the protection.

Claims (6)

1. the method for calcirm-fluoride finished product is prepared using calcium fluoride containing sludge, it is characterised in that including:
Mix calcium fluoride containing sludge and auxiliary agent A;The auxiliary agent A removes two with the silicon dioxde reaction in the calcium fluoride containing sludge Silica, is filtrated to get solution and sediment;The auxiliary agent A is for alkali lye or/and containing alkali waste water;
The sediment and auxiliary agent B are mixed, the auxiliary agent B turns into calcirm-fluoride with the calcium hydroxide reaction in the sediment;With Other hydroxide reactions, become solution, are removed;Obtain calcium fluoride precipitate after cleaning, filtering produce calcirm-fluoride into Product;The auxiliary agent B is hydrofluoric acid or/and the waste water of hydrofluoric acid containing;
The calcirm-fluoride finished product, its Calcium Fluoride Content is 95.0%~99.9%.
2. the method that utilization calcium fluoride containing sludge according to claim 1 prepares calcirm-fluoride finished product, it is characterised in that described The reaction temperature of silica in auxiliary agent A and the calcium fluoride containing sludge is normal temperature~150 DEG C.
3. the method that utilization calcium fluoride containing sludge according to claim 1 or 2 prepares calcirm-fluoride finished product, it is characterised in that The auxiliary agent A obtains waterglass with the silicon dioxde reaction in the calcium fluoride containing sludge.
4. the method that utilization calcium fluoride containing sludge according to claim 1 or 2 prepares calcirm-fluoride finished product, it is characterised in that The auxiliary agent A is sodium aluminate solution with the product that the aluminium hydroxide in the calcium fluoride containing sludge reacts.
5. the method that utilization calcium fluoride containing sludge according to claim 1 prepares calcirm-fluoride finished product, it is characterised in that described The reaction temperature of hydroxide in auxiliary agent B and the sediment is normal temperature~95 DEG C.
6. the method that utilization calcium fluoride containing sludge according to claim 1 prepares calcirm-fluoride finished product, it is characterised in that described Calcium fluoride containing sludge is the sediment after the neutralization reaction of fluoride waste calcium hydroxide is handled;CaF2 contains in the calcium fluoride sludge Measure as 50~80%wt, SiO2 contents are 1~30%wt, CaO content is 2~35%wt, and the contents of Al (OH) 3 are 0~20%wt, Surplus is other hydroxide.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109775743A (en) * 2019-03-22 2019-05-21 盛隆资源再生(无锡)有限公司 A method of sterling calcirm-fluoride is extracted from calcium fluoride sludge
CN111994937A (en) * 2020-08-31 2020-11-27 苏州中材非金属矿工业设计研究院有限公司 Method for recovering calcium fluoride from fluorine-containing sludge
CN112897562A (en) * 2021-01-05 2021-06-04 上海大学 Method for purifying calcium fluoride from calcium fluoride sludge
CN113753934A (en) * 2021-10-14 2021-12-07 湖北鑫熔生态科技新材料有限公司 Method for preparing 97% purity fluorite powder

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011125812A (en) * 2009-12-18 2011-06-30 Kobelco Eco-Solutions Co Ltd Method for treating wastewater containing fluorine and silicon, method for producing calcium fluoride, and apparatus for treating fluorine-containing wastewater
CN103232053A (en) * 2013-05-17 2013-08-07 北方民族大学 Method for producing calcium fluoride by bottom sludge generated during treatment of industrial fluoride-containing wastewater
CN105601066A (en) * 2016-03-18 2016-05-25 盐城工学院 Method for refining calcium fluoride from fluorine-containing sludge

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011125812A (en) * 2009-12-18 2011-06-30 Kobelco Eco-Solutions Co Ltd Method for treating wastewater containing fluorine and silicon, method for producing calcium fluoride, and apparatus for treating fluorine-containing wastewater
CN103232053A (en) * 2013-05-17 2013-08-07 北方民族大学 Method for producing calcium fluoride by bottom sludge generated during treatment of industrial fluoride-containing wastewater
CN105601066A (en) * 2016-03-18 2016-05-25 盐城工学院 Method for refining calcium fluoride from fluorine-containing sludge

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
何源 等: "氟化钙污泥处置及资源化利用", 《环境监测管理与技术》 *
谢明 等: "从含氟底泥中提取氟化钙的研究", 《无机盐工业》 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109775743A (en) * 2019-03-22 2019-05-21 盛隆资源再生(无锡)有限公司 A method of sterling calcirm-fluoride is extracted from calcium fluoride sludge
CN109775743B (en) * 2019-03-22 2021-11-30 盛隆资源再生(无锡)有限公司 Method for extracting pure calcium fluoride from calcium fluoride sludge
CN111994937A (en) * 2020-08-31 2020-11-27 苏州中材非金属矿工业设计研究院有限公司 Method for recovering calcium fluoride from fluorine-containing sludge
CN111994937B (en) * 2020-08-31 2023-11-03 苏州中材非金属矿工业设计研究院有限公司 Method for recycling calcium fluoride from fluorine-containing sludge
CN112897562A (en) * 2021-01-05 2021-06-04 上海大学 Method for purifying calcium fluoride from calcium fluoride sludge
CN113753934A (en) * 2021-10-14 2021-12-07 湖北鑫熔生态科技新材料有限公司 Method for preparing 97% purity fluorite powder

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Inventor after: Ying Shengrong

Inventor after: Wen Tao

Inventor after: Jiang Zhan

Inventor after: Ying Yue

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