CN106480507A - A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker - Google Patents

A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker Download PDF

Info

Publication number
CN106480507A
CN106480507A CN201611002654.3A CN201611002654A CN106480507A CN 106480507 A CN106480507 A CN 106480507A CN 201611002654 A CN201611002654 A CN 201611002654A CN 106480507 A CN106480507 A CN 106480507A
Authority
CN
China
Prior art keywords
ardealite
crystal whisker
calcium sulfate
low cost
new technology
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.)
Pending
Application number
CN201611002654.3A
Other languages
Chinese (zh)
Inventor
郑绍聪
闫宇星
王智娟
朱丽萍
林雪飞
汪帆
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yunnan Yuntian rengao Industrial Co. Ltd.
Original Assignee
Qujing Normal University
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 Qujing Normal University filed Critical Qujing Normal University
Priority to CN201611002654.3A priority Critical patent/CN106480507A/en
Publication of CN106480507A publication Critical patent/CN106480507A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B29/00Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape
    • C30B29/60Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape characterised by shape
    • C30B29/62Whiskers or needles
    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B29/00Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape
    • C30B29/10Inorganic compounds or compositions
    • C30B29/46Sulfur-, selenium- or tellurium-containing compounds
    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B7/00Single-crystal growth from solutions using solvents which are liquid at normal temperature, e.g. aqueous solutions
    • C30B7/10Single-crystal growth from solutions using solvents which are liquid at normal temperature, e.g. aqueous solutions by application of pressure, e.g. hydrothermal processes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker, comprises the steps:(1) adopt flotation desilication technology to remove quartz and partial impurities in ardealite, improve sulfate dihydrate calcium content >=92.0% in ardealite;In step(1)Its weight 0.5~2.0% dispersant, grinding 5~30min after mixing is added, it is standby that homogenizing process is prepared into solids content 5~12% in the upgrading ardealite obtaining;(3)Add its weight 0.1~5.0% crystal modifier and 1% sulphuric acid or hydrochloric acid in ardealite slurry, stir, proceed in pressure reaction still;(4)Crystal whisker of gypsum converts:120~140 DEG C of conversion temperature of setting, reacts temperature retention time 2.0h, after question response is complete, fast filtering, and dehydration, it is dried more than 80 DEG C of temperature, obtain final product hemihydrate calcium sulfate crystal whisker.Process is simple, low cost, gained Calcium Sulfate Whiskers are tiny, and draw ratio is high, and pattern is completely uniform.

Description

A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker
Technical field
The present invention relates to a kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker.
Background technology is led
Ardealite is the by-product during Wet-process phosphoric acid (WPPA).With the continuous increasing to high-concentration phosphate compound fertilizerses demand both at home and abroad Long, promote phosphoric acid by wet process industrial expansion, also create more ardealites.Therefore, the comprehensive resource profit to ardealite With having critically important resource and Significance for Environment.
Calcium sulfate crystal whiskers, call crystal whisker of gypsum, also known as gypsum fiber, white fluffy solid, refer under certain condition with The palpus shape monocrystal being shaped like chopped fiber of single crystal form growth, its intensity theoretical strength that valency is good for close between material atom. Its main character is as follows:(1)There is excellent mechanical property:Its section mostly is hexagon, rhomboid, triangle or strip shape, Different from the circular cross section of glass fibre etc., considerably increase draw ratio, increase plastics, fire-proof board draw ratio can be met (30-100)Requirement;Tensile strength is 5-10 times of glass fibre;Temperature does not decompose softening when raising, and intensity is almost lossless Lose, can be applicable to fire proofing material;No fatigue effect, be ground into powder, cut-out after, intensity is not also suffered a loss.(2)Have well Stability and the compatibility, excellent flatness, regenerability is good.(3)Toxicity is low:Compared with other whiskers, toxicity is minimum.(4)Become This is low:Calcium sulfate crystal whiskers internal price is 6-12 unit/kg, the only 1/300-1/200 of silicon carbide whisker.Building, Medicine, plastics, rubber and field of environment protection have important purposes, are more used as composite reinforcing component at present.
Publication No. CN102115142A Chinese invention patent, discloses a kind of preparation method of industrial sulphuric acid calcium.The party With ardealite as raw material, first washing removes soluble impurity to method, recycles excessive hydrochloric acid to remove insoluble phosphate with other not Solubility impurity, last filtration separation purified after industrial sulphuric acid calcium.The method needs to remove dephosphorization stone using excessive hydrochloric acid Silicon dioxide in cream, to improve the content of calcium sulphate dihydrate in ardealite.Publication No. CN104562180A Chinese invention is special Profit, discloses a kind of method of use preparing calcium sulphate whiskers from ardealite.The method with ardealite breeze and diluted acid, in uniform temperature Lower reaction, the calcium sulphate dihydrate in ardealite is completely dissolved in diluted acid, then makes the side of calcium sulphate dihydrate recrystallization by cooling Method prepares calcium sulfate crystal whiskers.The method needs a large amount of Ore Leachings, and serious to equipment corrosion, the crystallization time is long, subsequently simultaneously The product pH substantial amounts of fresh water (FW) of relatively low needs obtaining is washed, and has greater environmental impacts.
In sum, forefathers are made that fruitful work in terms of preparing calcium sulphate whiskers from ardealite, but remain work The shortcomings of skill is complicated, crystal whisker products are unstable, production cost is high.
Content of the invention
It is an object of the invention to provide a kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker, existing to solve There is problem present in technology.
Technical scheme:
A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker, comprises the steps:
(1), using quartz and partial impurities in ardealite, there is floatability, ardealite removed using flotation desilication technology In quartz and partial impurities, improve ardealite in sulfate dihydrate calcium content >=92.0%;
(2), in step(1)In the upgrading ardealite obtaining plus its weight 0.5~2.0% dispersant, grinding 5 after mixing~ 30min, it is standby that homogenizing process is prepared into solids content 5~12% slurry;Preferably, homogenizing is processed is prepared into solids content 10% Slurry;Described dispersant be one of technical grade sodium pyrophosphate, sodium hexameta phosphate, polyacrylamide or lignin sodium sulfonate or Several mixing.
(3), to step(2)It is obtained in ardealite slurry and add this slurry weight 0.1~5.0% crystal modifier and 1% industry Level sulphuric acid or hydrochloric acid, and adjust pH value 2~5, stir to material uniformly, then proceed in pressure reaction still;
(4)Crystal whisker of gypsum converts:120~140 DEG C of conversion temperature of setting, reacts temperature retention time 2.0h, after question response is complete, quickly Filter, dehydration, be dried more than 80 DEG C of temperature, obtain final product hemihydrate calcium sulfate crystal whisker.Wherein filtrate contains crystal modifier and sulphuric acid, returns step Suddenly(2)Middle continuation recycles.
Described crystal modifier is inorganic salt or organic additive, wherein:Inorganic salt is sodium chloride, potassium chloride, zinc chloride, chlorination One in magnesium, sodium sulfate, potassium sulfate, zinc sulfate, magnesium sulfate, aluminum sulfate, sodium phosphate, potassium phosphate, zinc phosphate, magnesium phosphate and aluminum phosphate Plant or multiple combinations;Organic additive is cetyl trimethylammonium bromide, dodecylbenzene sodium sulfonate, hexadecyl hydrosulfate The combination of one or more of sodium, Oleic acid and enuatrol;The aforementioned inorganic salt as crystal modifier or organic additive are work Industry level commercial sources.
The hemihydrate calcium sulfate crystal whisker being obtained in aforementioned manners, sulfate hemihydrate calcium content >=92.00%(wt%), whiteness is more than 92%, loose thickness:0.1~0.3g/cm3, whisker length:20~500um, diameter of whiskers:1~4um, draw ratio 10~100. It is process is simple that the present invention prepares the maximum feature of hemihydrate calcium sulfate crystal whisker, low production cost, and prepared calcium sulfate crystal whiskers have Diameter is tiny, and draw ratio is high, and pattern is completely uniform.Can as to whiteness require be not particularly harsh Colophonium, plastics, rubber, The reinforcing material additive of the industry such as brake block and pottery, has broad application prospects.
The technical advantage of the present invention:Using gypsum grinding homogenizing treatment technology, increased Gypsum Fibrosum conversion ratio.Adopted by contrast With homogenizing technology and the semi-hydrated gypsum whisker SEM spectrum being provided without uniform technology, result illustrates, solves Gypsum Fibrosum using this technology brilliant The uneven technical problem of whisker in palpus preparation process, this technology has low cost and the uniform feature of slurry.
Brief description
Fig. 1 prepares sulfate hemihydrate whisker process chart for ardealite.
Specific embodiment
Example 1 is to prepare semi-hydrated gypsum whisker without the ardealite that homogenizing is processed:
Processing step is as follows:
(1)Remove quartz and the partial impurities in ardealite using common flotation desilication technology, improve sulfate dihydrate in ardealite Calcium content >=92.0%.
(2)It is 5% slip that the ardealite of upgrading and water are prepared solid masses concentration, adds slurry weight 0.5% magnesium sulfate Sulphuric acid with 1%, carries out hydro-thermal reaction 2.0h under the conditions of 120 DEG C~140 DEG C, after question response is complete, fast filtering, and dehydration, It is dried, obtain final product hemihydrate calcium sulfate crystal whisker.Result shows, prepares semi-hydrated gypsum whisker, whisker without the ardealite that homogenizing is processed There are unreacted impurity and speckle in product, whisker morphology is also uneven, have a strong impact on semi-hydrated gypsum crystal whisker products quality.
Example 2 prepares semi-hydrated gypsum whisker without the ardealite that homogenizing is processed:
Processing step is as follows:
(1)Remove quartz and the partial impurities in ardealite using common flotation desilication technology, improve sulfate dihydrate in ardealite Calcium content >=92.0%.
(2)It is 12% slip that the ardealite of upgrading and water are prepared solid masses concentration, adds 1.5% sulfur based on its weight Sour aluminum and 1% sulphuric acid, carry out hydro-thermal reaction 2.0h under the conditions of 120 DEG C~140 DEG C, after question response is complete, fast filtering, take off Water, is dried, obtains final product hemihydrate calcium sulfate crystal whisker.Result shows, prepares semi-hydrated gypsum whisker without the ardealite that homogenizing is processed, brilliant Must there are unreacted impurity and speckle, whisker morphology is also uneven, has a strong impact on semi-hydrated gypsum crystal whisker products quality in product.
Semi-hydrated gypsum whisker prepared by the ardealite that example 3 is processed through homogenizing:
Processing step is as follows:
(1)Remove quartz and the partial impurities in ardealite using common flotation desilication technology, improve sulfate dihydrate in ardealite Calcium content >=92.0%.
(2)Upgrading ardealite is processed through grinding 10min homogenizing and is prepared into solids content 8% slip, standby;
(3)By solid masses concentration be 8% slip add based on its weight 2.0% iron sulfate and 1% sulphuric acid, 120 DEG C~140 Carry out hydro-thermal reaction 2.0h under the conditions of DEG C, after question response is complete, fast filtering, dehydration, it is dried, obtain final product hemihydrate calcium sulfate crystal whisker. Result shows, semi-hydrated gypsum whisker prepared by the ardealite processing through homogenizing, and crystal whisker products pattern uniformly, has no speckle impurity, Solve the problems, such as homogenizing in crystal whisker products production process.
Semi-hydrated gypsum whisker prepared by the ardealite that example 4 is processed through homogenizing:
Processing step is as follows:
(1)Remove quartz and the partial impurities in ardealite using common flotation desilication technology, improve sulfate dihydrate in ardealite Calcium content >=92.0%.
(2)Upgrading ardealite is processed through grinding 30min homogenizing and is prepared into solids content 10% slip, standby;
(3)Solid masses concentration is that 10% slip adds its weight meter 4.0% aluminum phosphate and 1% sulphuric acid, 120 DEG C~140 Carry out hydro-thermal reaction 2.0h under the conditions of DEG C, after question response is complete, fast filtering, dehydration, it is dried, obtain final product hemihydrate calcium sulfate crystal whisker. Result shows, semi-hydrated gypsum whisker prepared by the ardealite processing through homogenizing, and crystal whisker products pattern uniformly, has no speckle impurity, Solve the problems, such as homogenizing in crystal whisker products production process.
Semi-hydrated gypsum whisker prepared by the ardealite that example 5 is processed through homogenizing:
Processing step is as follows:
(1)Remove quartz and the partial impurities in ardealite using common flotation desilication technology, improve sulfate dihydrate in ardealite Calcium content >=92.0%.
(2)Upgrading ardealite is processed through grinding 5min homogenizing and is prepared into solids content 6% slip, standby;
(3)Solid masses concentration is added its weight meter 1.5% magnesium sulfate and 1% sulphuric acid for 6% slip, in 120 DEG C~140 DEG C bars Carry out hydro-thermal reaction 2.0h under part, after question response is complete, fast filtering, dehydration, it is dried, obtain final product hemihydrate calcium sulfate crystal whisker.Result Show, semi-hydrated gypsum whisker prepared by the ardealite processing through homogenizing, crystal whisker products pattern uniformly, has no speckle impurity, solve Homogenizing problem in crystal whisker products production process.

Claims (6)

1. a kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker is it is characterised in that comprise the steps:
(1)Using quartz and partial impurities in ardealite, there is floatability, ardealite is removed using flotation desilication technology In quartz and partial impurities, improve ardealite in sulfate dihydrate calcium content >=92.0%;
(2)In step(1)Its weight 0.5~2.0% dispersant is added in the upgrading ardealite obtaining, grinding 5 after mixing~ 30min, it is standby that homogenizing process is prepared into solids content 5~12%;
(3)To step(2)It is obtained in ardealite slurry and add this slurry weight 0.1~5.0% crystal modifier and 1% technical grade sulfuric acid Or hydrochloric acid, and adjust pH value 2~5, stir to material uniformly, then proceed in pressure reaction still;
(4)Crystal whisker of gypsum converts:120~140 DEG C of conversion temperature of setting, reacts temperature retention time 2.0h, after question response is complete, quickly Filter, dehydration, be dried more than 80 DEG C of temperature, obtain final product hemihydrate calcium sulfate crystal whisker.
2. the new technology of a kind of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker according to claim 1, its feature exists It is sodium chloride, potassium chloride, zinc chloride, magnesium chloride, sodium sulfate, potassium sulfate, zinc sulfate, sulphuric acid in the inorganic salt as crystal modifier One or more of combination in magnesium, aluminum sulfate, sodium phosphate, potassium phosphate, zinc phosphate, magnesium phosphate and aluminum phosphate.
3. the new technology of a kind of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker according to claim 1, its feature exists It is cetyl trimethylammonium bromide, dodecylbenzene sodium sulfonate, hexadecyl hydrosulfate in the organic additive as crystal modifier The combination of one or more of sodium, Oleic acid and enuatrol.
4. the new technology of the inexpensive hemihydrate calcium sulfate crystal whisker of a kind of ardealite preparation according to claim 1,2 or 3, it is special Levy and be that the aforementioned inorganic salt as crystal modifier or organic additive are technical grade commercial sources.
5. the new technology of a kind of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker according to claim 1, its feature exists In step(2)Middle homogenizing processes and is prepared into solids content 10% slurry.
6. the new technology of a kind of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker according to claim 1, its feature exists In step(4)The filtrate being filtrated to get is back to step(2)In, continue cycling through use.
CN201611002654.3A 2016-11-15 2016-11-15 A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker Pending CN106480507A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611002654.3A CN106480507A (en) 2016-11-15 2016-11-15 A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611002654.3A CN106480507A (en) 2016-11-15 2016-11-15 A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker

Publications (1)

Publication Number Publication Date
CN106480507A true CN106480507A (en) 2017-03-08

Family

ID=58272039

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611002654.3A Pending CN106480507A (en) 2016-11-15 2016-11-15 A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker

Country Status (1)

Country Link
CN (1) CN106480507A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107190325A (en) * 2017-05-09 2017-09-22 武汉理工大学 A kind of method that utilization industrial by-product ardealite prepares anhydrous calcium sulfate whisker
CN108411369A (en) * 2018-04-11 2018-08-17 中国计量大学 A method of utilizing preparing alpha-hemihydrate gypsum with desulfurated gypsum whisker in alcohol-water system
CN109280959A (en) * 2017-07-19 2019-01-29 北新集团建材股份有限公司 A method of semi-hydrated gypsum fiber is prepared by desulfurized gypsum
CN109280979A (en) * 2017-07-19 2019-01-29 北新集团建材股份有限公司 A method of preparing semi-hydrated gypsum whisker
CN110205671A (en) * 2019-07-04 2019-09-06 江苏一夫科技股份有限公司 It is a kind of to prepare Dihydrate gypsum whiskers, the method for hemihydrate calcium sulfate crystal whisker and product as made from it
CN110699756A (en) * 2019-10-31 2020-01-17 江西富达盐化有限公司 Method for preparing alpha-type gypsum whisker by using ammonia-soda waste liquid
CN110835780A (en) * 2019-10-28 2020-02-25 昆明理工大学 Method for preparing nanometer α type calcium sulfate hemihydrate crystal whisker from phosphogypsum in reverse microemulsion system
CN111286788A (en) * 2020-02-27 2020-06-16 武汉工程大学 Method for preparing calcium sulfate whisker by phosphogypsum hydrothermal method
CN111560521A (en) * 2020-06-22 2020-08-21 湖南科技大学 Method for efficiently leaching valuable metal impurities in phosphogypsum and preparing high-added-value gypsum product
CN113830814A (en) * 2021-09-16 2021-12-24 浙江钙宝新材料有限公司 Method for preparing calcium sulfate nano-rods from industrial solid waste gypsum
CN114538840A (en) * 2022-03-19 2022-05-27 青岛惠城环保科技股份有限公司 Preparation method of high-strength anti-freezing foam concrete with in-situ generated whiskers
CN115872435A (en) * 2022-09-20 2023-03-31 四川大学 Method for preparing high-purity gypsum through crystal phase reconstruction

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101792932A (en) * 2009-11-16 2010-08-04 瓮福(集团)有限责任公司 Method for preparing ultra-fine calcium sulfate crystal whisker by using phosphogypsum
CN104005086A (en) * 2014-04-04 2014-08-27 贵阳中化开磷化肥有限公司 Method for preparing calcium sulfate dihydrate crystal whisker from phosphorus gypsum
CN104562180A (en) * 2015-01-07 2015-04-29 西南科技大学 Method for preparing calcium sulfate whisker from phosphogypsum
CN105350066A (en) * 2015-12-15 2016-02-24 云南省化工研究院 Method for preparing calcium sulfate hemihydrate crystal whisker by ardealite

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101792932A (en) * 2009-11-16 2010-08-04 瓮福(集团)有限责任公司 Method for preparing ultra-fine calcium sulfate crystal whisker by using phosphogypsum
CN104005086A (en) * 2014-04-04 2014-08-27 贵阳中化开磷化肥有限公司 Method for preparing calcium sulfate dihydrate crystal whisker from phosphorus gypsum
CN104562180A (en) * 2015-01-07 2015-04-29 西南科技大学 Method for preparing calcium sulfate whisker from phosphogypsum
CN105350066A (en) * 2015-12-15 2016-02-24 云南省化工研究院 Method for preparing calcium sulfate hemihydrate crystal whisker by ardealite

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107190325A (en) * 2017-05-09 2017-09-22 武汉理工大学 A kind of method that utilization industrial by-product ardealite prepares anhydrous calcium sulfate whisker
CN107190325B (en) * 2017-05-09 2019-10-25 武汉理工大学 A method of anhydrous calcium sulfate whisker is prepared using industrial by-product ardealite
CN109280959A (en) * 2017-07-19 2019-01-29 北新集团建材股份有限公司 A method of semi-hydrated gypsum fiber is prepared by desulfurized gypsum
CN109280979A (en) * 2017-07-19 2019-01-29 北新集团建材股份有限公司 A method of preparing semi-hydrated gypsum whisker
CN108411369A (en) * 2018-04-11 2018-08-17 中国计量大学 A method of utilizing preparing alpha-hemihydrate gypsum with desulfurated gypsum whisker in alcohol-water system
CN110205671A (en) * 2019-07-04 2019-09-06 江苏一夫科技股份有限公司 It is a kind of to prepare Dihydrate gypsum whiskers, the method for hemihydrate calcium sulfate crystal whisker and product as made from it
CN110835780B (en) * 2019-10-28 2021-11-09 昆明理工大学 Method for preparing nano-scale alpha type calcium sulfate hemihydrate crystal whisker from phosphogypsum in reverse microemulsion system
CN110835780A (en) * 2019-10-28 2020-02-25 昆明理工大学 Method for preparing nanometer α type calcium sulfate hemihydrate crystal whisker from phosphogypsum in reverse microemulsion system
CN110699756B (en) * 2019-10-31 2021-06-25 江西富达盐化有限公司 Method for preparing alpha-type gypsum whisker by using ammonia-soda waste liquid
CN110699756A (en) * 2019-10-31 2020-01-17 江西富达盐化有限公司 Method for preparing alpha-type gypsum whisker by using ammonia-soda waste liquid
CN111286788A (en) * 2020-02-27 2020-06-16 武汉工程大学 Method for preparing calcium sulfate whisker by phosphogypsum hydrothermal method
CN111560521A (en) * 2020-06-22 2020-08-21 湖南科技大学 Method for efficiently leaching valuable metal impurities in phosphogypsum and preparing high-added-value gypsum product
CN111560521B (en) * 2020-06-22 2021-08-10 湖南科技大学 Method for efficiently leaching valuable metal impurities in phosphogypsum and preparing high-added-value gypsum product
CN113830814A (en) * 2021-09-16 2021-12-24 浙江钙宝新材料有限公司 Method for preparing calcium sulfate nano-rods from industrial solid waste gypsum
CN114538840A (en) * 2022-03-19 2022-05-27 青岛惠城环保科技股份有限公司 Preparation method of high-strength anti-freezing foam concrete with in-situ generated whiskers
CN115872435A (en) * 2022-09-20 2023-03-31 四川大学 Method for preparing high-purity gypsum through crystal phase reconstruction
CN115872435B (en) * 2022-09-20 2024-05-14 四川大学 Method for preparing high-purity gypsum by crystal phase reconstruction

Similar Documents

Publication Publication Date Title
CN106480507A (en) A kind of new technology of ardealite preparation low cost hemihydrate calcium sulfate crystal whisker
US10696552B2 (en) Method for producing wet-process phosphoric acid and by-producing alpha-hemihydrate gypsum and high-purity and high-whiteness alpha-hemihydrate gypsum
CN111348632B (en) Method for producing semi-hydrated phosphoric acid and co-producing alpha-type high-strength gypsum from phosphorite
CN103508689B (en) A kind of low cost prepares the method for alpha semi-hydrated gypsum and prepared alpha semi-hydrated gypsum and gypsum block
CN102925956B (en) Method for preparing calcium sulfate hemihydrate whiskers by taking ardealite as main raw material
CN105154979B (en) A kind of method for producing phosphoric acid by wet process by-product αsemiwatergypsum whisker and the high whiteness αsemiwatergypsum whisker of high-purity
KR880007358A (en) Manufacturing method of high concentration phosphoric acid
CN101734701B (en) Method for producing cryolite by using fluorine-containing slag of electrolytic aluminum
CN105174270A (en) Technology for preparing sodium fluorosilicate through fluoride-containing wastewater
CN106587679B (en) A kind of building gypsum plaster and preparation method thereof using bunt gypsum production
CN105350066B (en) A kind of method that ardealite prepares hemihydrate calcium sulfate crystal whisker
CN106400118A (en) Surface modification method for preparing anhydrous calcium sulfate whisker difficult to dissolve in water
CN115676788B (en) High-purity potassium dihydrogen phosphate and preparation method thereof
CN105645454B (en) A kind of preparation of column semi-hydrated gypsum and filtrate processing method
CN115043619B (en) Preparation method of self-gelling fiber composite material
CN106587678B (en) A kind of reclaimed gypsum powder and preparation method thereof for construction wall
CN112047422B (en) Production process of composite phosphorus removal agent for sewage treatment
CN107352926A (en) A kind of method that artificial stone is produced using discarded slurry
CN103803517B (en) The method of the low silicon ardealite of high silicon Phosphate Rock acid by-product
US4113835A (en) Process for preparing pure synthetic calcium sulfate semihydrate
CN108383484B (en) Partition wall batten prepared from red mud and preparation method thereof
CN103526277B (en) A kind of cross section of manufacturing is hexagon and the method with low phosphorus content crystal whisker of gypsum
CN1064330C (en) Method for leaching phosphate from low-grade powdered rock phosphate
CN108236937B (en) Preparation method of hydrated calcium chloroaluminate
CN101289214B (en) Process for preparing cryolite

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right

Effective date of registration: 20181228

Address after: 655011 Qujing Normal College of Sanjiang Avenue, Qilin District, Qujing City, Yunnan Province

Applicant after: Qujing Normal University

Applicant after: Yunnan Yuntian rengao Industrial Co. Ltd.

Address before: 655011 Qujing Normal College of Sanjiang Avenue, Qilin District, Qujing City, Yunnan Province

Applicant before: Qujing Normal University

TA01 Transfer of patent application right
RJ01 Rejection of invention patent application after publication

Application publication date: 20170308

RJ01 Rejection of invention patent application after publication