CN109651846B - Post-treatment method of rare earth sulfide - Google Patents

Post-treatment method of rare earth sulfide Download PDF

Info

Publication number
CN109651846B
CN109651846B CN201811622624.1A CN201811622624A CN109651846B CN 109651846 B CN109651846 B CN 109651846B CN 201811622624 A CN201811622624 A CN 201811622624A CN 109651846 B CN109651846 B CN 109651846B
Authority
CN
China
Prior art keywords
rare earth
earth sulfide
primary powder
mass
mixed solution
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.)
Active
Application number
CN201811622624.1A
Other languages
Chinese (zh)
Other versions
CN109651846A (en
Inventor
刘建钢
翟纪敏
魏亮
张�成
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.)
Baotou Hongbo Te Technology Co ltd
Original Assignee
Baotou Hongbo Te Technology Co ltd
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 Baotou Hongbo Te Technology Co ltd filed Critical Baotou Hongbo Te Technology Co ltd
Publication of CN109651846A publication Critical patent/CN109651846A/en
Application granted granted Critical
Publication of CN109651846B publication Critical patent/CN109651846B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C1/00Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C3/00Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
    • C09C3/006Combinations of treatments provided for in groups C09C3/04 - C09C3/12
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C3/00Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
    • C09C3/04Physical treatment, e.g. grinding, treatment with ultrasonic vibrations
    • C09C3/041Grinding
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C3/00Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
    • C09C3/06Treatment with inorganic compounds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C3/00Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
    • C09C3/08Treatment with low-molecular-weight non-polymer organic compounds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C3/00Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
    • C09C3/12Treatment with organosilicon compounds

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Pigments, Carbon Blacks, Or Wood Stains (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

The invention provides a post-treatment method of rare earth sulfide, which is characterized in that the prepared rare earth sulfide primary powder is treated by the steps of the invention, and the pigment has bright color, strong tinting strength and covering power, good chemical stability and good heat resistance.

Description

Post-treatment method of rare earth sulfide
Technical Field
The invention relates to the technical field of chemical industry, in particular to a post-treatment method of rare earth sulfide.
Background
With the increasing environmental protection situation, in recent years, many countries have made strict regulations to limit or prohibit the use of toxic pigments that pollute the environment, and colored inorganic pigments containing toxic heavy metals such as cadmium, chromium, lead, etc. that are being used in large quantities in the market are being eliminated. In the last 90 th century, marking paints on roads are regulated by legislation in countries such as Europe and America to be lead-free, and in the European Union of the last year, all red and yellow pigments are regulated not to contain cadmium. Therefore, the development of green, non-toxic and pollution-free high-performance red and yellow pigments is imminent.
The rare earth sulfide pigment is an environment-friendly inorganic pigment without heavy metals, is insoluble in water and strong alkaline solution, is easily soluble in acid and releases hydrogen sulfide gas, and has the chemical stability of 1500 ℃ in inert gas and reducing atmosphere and 350 ℃ in oxidizing atmosphere. In recent years, rare earth sulfide pigment has bright color and good weather resistance, so that the rare earth sulfide pigment is used as an environment-friendly color pigment in the fields of plastics, coatings and the like to replace toxic heavy metal pigment.
The most widely used preparation methods of rare earth sulfide pigments are two: one is a solid-solid synthesis method, and the other is a gas-solid synthesis method. The rare earth sulfide pigment synthesized by any method has the defects of poor tinting strength and covering power, low thermal stability and poor acid resistance.
Disclosure of Invention
Therefore, the present invention aims to obtain a rare earth sulfide for pigments which is non-toxic, has good dispersibility, and has improved tinting strength, hiding power, thermal stability and acid resistance, without affecting the color of the rare earth sulfide pigment itself.
The above object of the present invention is achieved by the following technical solutions:
a method for post-treatment of rare earth sulfides, the method comprising the steps of:
(1) mixing the rare earth sulfide primary powder with water to obtain a mixed solution; adding a flotation agent into the mixed solution, grinding and mixing in a colloid mill, removing floating aggregates during grinding, and filtering to obtain a filter cake.
(2) Washing the filter cake obtained in the step (1) with an alcoholic solution, mixing and stirring the washed filter cake and the alcoholic solution, adding a dispersing agent in the stirring process, and then grinding the mixture under an oxygen-free condition until the particle size of the rare earth sulfide in the mixed solution is 100-3000 nm;
(3) after the step (2) is finished, adding a fluorinating agent into the mixed solution for fluorination treatment;
(4) after the fluorination treatment in the step (3) is finished, adding zinc oxide and a catalyst into the mixed solution;
(5) immediately adding a transparent oxide precursor into the mixed solution after the step (4) is finished, and stirring for 1-3h at the speed of 100-1000 g/min;
(6) after the step (5) is finished, filtering, washing with alcohol and drying to obtain dry rare earth sulfide;
(7) and (4) screening the dried rare earth sulfide obtained in the step (6) by using a centrifugal screen to obtain a product.
Preferably, in the step (1), the rare earth sulfide primary powder is a primary powder of cerium sulfide, lanthanum cerium sulfide or samarium sulfide; more preferably, the rare earth sulfide primary powder is cerium sulfide primary powder;
preferably, in the step (1), the mass ratio of the rare earth sulfide primary powder to water is 1: 1-5;
preferably, in step (1), the flotation agent is kerosene, diesel oil, vegetable oil;
preferably, in the step (1), the mass of the flotation agent is 3% -9% of the mass of the rare earth sulfide primary powder, and more preferably 5%;
preferably, in the step (1), the floating aggregate is an aggregate of the carbon powder and the flotation agent in the primary powder;
preferably, in step (2), the alcohol solution is selected from methanol, ethanol or butanol, more preferably 99% ethanol;
preferably, in the step (2), the mass of the alcohol solution for mixing with the filter cake is 2-10 times, more preferably 3 times that of the rare earth sulfide primary powder;
preferably, in step (2), the dispersant is a nonionic water-soluble or organic solvent-soluble polymer; more preferably cellulose and its derivatives, polyvinylamides, polyethylene oxides, polyethylene glycols, polyoxyethylenated polyoxypropylene glycols, polyacrylates, polyoxyethylenated acid esters, polyoxyethylenated alkylphenols, polyvinyl alcohols, alkanolamides, polyvinylpyrrolidone or xanthan gum-based compounds, more preferably polyvinylpyrrolidone;
preferably, in the step (2), the mass of the dispersing agent is 0.5-5% of the mass of the rare earth sulfide primary powder, and more preferably is 2%;
preferably, in step (2), the particle size is 300-800nm, preferably 500 nm;
preferably, in step (3), the fluorinating agent is a solid, liquid or gaseous fluorinating agent, more preferably a liquid or gaseous fluorinating agent;
preferably, in step (3), the fluorinating agent is selected from fluorine gas, hydrofluoric acid, ammonium fluoride, alkali metal fluoride or nitrogen fluoride, more preferably ammonium fluoride;
preferably, in the step (3), the mass of the fluorinating agent is 1-20% of that of the rare earth sulfide primary powder, and more preferably 5%;
preferably, in step (4), the zinc oxide has a particle size of less than 40 μm, more preferably 500 nm;
preferably, in the step (4), the mass of the zinc oxide is 1-15% of the mass of the rare earth sulfide primary powder; more preferably 5%;
preferably, in the step (4), the catalyst is ammonia water, sodium hydroxide, potassium hydroxide or sodium carbonate, and more preferably, ammonia water;
preferably, in the step (4), the mass of the catalyst is 5-60% of the mass of the rare earth sulfide primary powder; more preferably 25%;
preferably, in step (5), the transparent oxide precursor is selected from one or more of ethyl silicate (corresponding to silica), aluminum sulfate (corresponding to alumina), zirconium sulfate (corresponding to zirconia), calcium sulfate (corresponding to calcium oxide) or rare earth sulfate (corresponding to rare earth metal oxide); more preferably, the transparent oxide precursor is selected from ethyl silicate;
preferably, in the step (5), the mass of the transparent oxide precursor is 5-50% of the mass of the rare earth sulfide primary powder; more preferably 15%;
preferably, during step (5) the temperature is maintained at 10-40 ℃, more preferably at 25 ℃; maintaining a pH of 8-10, more preferably 9;
preferably, in step (7), the screen size of the centrifugal screen is 10-100 μm, more preferably 45 μm.
In a particular embodiment, the fluorination treatment of step (3) is carried out using the following conditions:
Ce2S3slurry concentration (which refers to a mixture obtained after the treatment in the step (2), namely rare earth sulfide, alcoholic solution and dispersing agent): 300-500 g/L;
NH4F solution concentration: 120-180 g/L;
and (4) treating the pH: more than 8 to 10;
treatment temperature: more than 20-30 ℃;
treatment time: 100 and 120 min.
In another specific embodiment, step (6) is performed after step (5) is performed 2 or more times, and when step (6) is performed after step (5) is performed 2 or more times, the transparent oxide precursor used in each execution of step (5) may be the same or different.
In yet another specific embodiment, step (5) is performed 2 times before step (6), wherein the transparent oxide precursor used in the first step (5) is ethyl silicate (corresponding to silica) and the transparent oxide precursor used in the second step (5) is aluminum sulfate (corresponding to alumina).
The rare earth sulfide pigment obtained by the post-treatment method has bright color, less carbon particle impurities, no larger particles in materials, uniform particle size distribution, improved tinting strength and covering power, improved ultraviolet resistance and weather resistance, good chemical stability and heat resistance of the obtained product, incomparable with organic red pigments, no heavy metal and environmental protection.
Detailed Description
The present invention is described in further detail below with reference to specific embodiments, which are given for the purpose of illustration only and are not intended to limit the scope of the invention.
Unless otherwise stated, the rare earth sulfide primary powders described in the following examples were prepared by the following steps:
1) uniformly mixing a rare earth compound and an additive, and filling the mixture into a reaction container, wherein the rare earth compound is cerium carbonate, the additive is sodium carbonate, and the addition ratio of the additive is that the molar ratio of Na to Ce is 0.8;
2) introducing inert gas into the reaction vessel to displace air in the reactor, and introducing mixed sulfur source gas of hydrogen sulfide and carbon disulfide after 30min, wherein the addition ratio of the gas sulfur source is that the molar ratio of S/Ce is 3;
3) heating from room temperature to 500 deg.C at a speed of 10 deg.C/min, maintaining for 60 min, heating to 900 deg.C at a speed of 10 deg.C/min, and maintaining for 120 min.
Example 1
(1) Mixing and grinding 400g of cerium sulfide primary powder and 1200g of water in a colloid mill, then adding 20g of kerosene, fishing out the kerosene and carbon powder after 5 minutes until no kerosene and carbon powder float on the surface of the mixed solution, and then filtering to obtain a filter cake;
(2) washing the filter cake obtained in the step (1) with 95% ethanol, mixing the washed filter cake with 95% ethanol according to the mass ratio of 1:2, adding 8g of PVP (polyvinylpyrrolidone) dispersing agent, and reducing the particle size of the pigment to 500nm by using a sand mill under the protection of nitrogen;
(3) then adding 20g of ammonium fluoride into the mixed solution at the temperature of 20-30 ℃ and reacting for 2 h;
(4) then adding 20g of zinc oxide and 200g of ammonia water into the mixed solution;
(5) adding 60g of tetraethoxysilane into the mixed solution within 2 hours, and stirring for 2 hours;
(6) then filtering, washing and drying;
(7) and (4) sieving the dried material by a 45-micron centrifugal sieve to obtain the product.
Example 2
(1) Mixing and grinding 400g of cerium sulfide primary powder and 1200g of water in a colloid mill, then adding 20g of kerosene, fishing out the kerosene and carbon powder after 5 minutes until no kerosene and carbon powder float on the surface of the mixed solution, and then filtering to obtain a filter cake;
(2) washing the filter cake obtained in the step (1) with 95% ethanol, mixing the washed filter cake with 95% ethanol according to the mass ratio of 1:2, adding 8g of PVP dispersant, and reducing the particle size of the pigment to 4000nm by using a sand mill under the protection of nitrogen;
steps (3) to (7) were the same as in example 1.
Example 3
(1) Mixing and grinding 400g of cerium sulfide primary powder and 1200g of water in a colloid mill, then adding 20g of kerosene, fishing out the kerosene and carbon powder after 5 minutes until no kerosene and carbon powder float on the surface of the mixed solution, and then filtering to obtain a filter cake;
(2) washing the filter cake obtained in the step (1) with 95% ethanol, mixing the washed filter cake with 95% ethanol according to the mass ratio of 1:2, adding 8g of PVP dispersant, and reducing the particle size of the pigment to 2000nm by using a sand mill under the protection of nitrogen;
steps (3) to (7) were the same as in example 1.
The coloring power of the products prepared in examples 1 to 3 was measured, and the results are shown in the following table:
examples Coloring power
1 100
2 50
3 80
Example 4
Steps (1) to (3) are the same as in example 1;
only adding 20g of zinc oxide into the mixed solution when the step (4) is carried out, and not adding ammonia water;
steps (5) to (7) were the same as in example 1.
Example 5
Steps (1) to (3) are the same as in example 1;
adding 20g of zinc oxide and 50g of ammonia water into the mixed solution;
steps (5) to (7) were the same as in example 1.
Example 6
Steps (1) to (4) are the same as in example 1;
stirring for 2 hours only in the step (5), and adding no tetraethoxysilane;
steps (6) to (7) were the same as in example 1.
Example 7
Steps (1) to (4) are the same as in example 1;
step (5) adding 28g of tetraethoxysilane into the mixed solution within 2 hours, and stirring for 2 hours;
steps (6) to (7) were the same as in example 1.
The temperature resistance and H of the products obtained in examples 1 and 4 to 7 were measured2S release, results are shown in the following table:
examples Temperature resistance (DEG C) H2S burst size (ppm)
1 320 95
4 240 505
5 280 280
6 240 610
7 280 290

Claims (10)

1. A method for post-treatment of rare earth sulfides, the method comprising the steps of:
(1) mixing the rare earth sulfide primary powder with water to obtain a mixed solution; adding a flotation agent into the mixed solution, grinding and mixing in a colloid mill, removing floating aggregates in the grinding process, and filtering to obtain a filter cake;
(2) washing the filter cake obtained in the step (1) with an alcoholic solution, mixing and stirring the washed filter cake and the alcoholic solution, adding a dispersing agent in the stirring process, and then grinding the mixture under an oxygen-free condition until the particle size of the rare earth sulfide in the mixed solution is 500 nm;
(3) after the step (2) is finished, adding a fluorinating agent into the mixed solution for fluorination treatment;
(4) after the fluorination treatment in the step (3) is finished, adding zinc oxide and a catalyst into the mixed solution;
(5) immediately adding a transparent oxide precursor into the mixed solution after the step (4) is finished, and stirring for 1-3h at the speed of 100-1000 g/min;
(6) after the step (5) is finished, filtering, washing and drying to obtain dry rare earth sulfide;
(7) screening the dried rare earth sulfide obtained in the step (6) by a centrifugal screen to obtain a product
In the step (1), the rare earth sulfide primary powder is cerium sulfide primary powder; the flotation agent is kerosene, and the mass of the flotation agent is 5% of that of the rare earth sulfide primary powder; the floating aggregate is an aggregate of carbon powder and a flotation agent in the primary powder;
in the step (2), the alcoholic solution is ethanol; the mass of the alcohol solution for mixing with the filter cake is 2 times of the mass of the primary powder of the rare earth sulfide; the dispersing agent is polyvinylpyrrolidone; the mass of the dispersing agent is 2% of that of the rare earth sulfide primary powder;
in step (3), the fluorinating agent is ammonium fluoride; the mass of the fluorinating agent is 5% of that of the rare earth sulfide primary powder;
in the step (4), the mass of the zinc oxide is 5% of that of the rare earth sulfide primary powder; the catalyst is ammonia water; the mass of the catalyst is 50% of that of the rare earth sulfide primary powder;
in the step (5), the transparent oxide precursor is selected from ethyl silicate.
2. The method according to claim 1, wherein in the step (1), the mass ratio of the rare earth sulfide primary powder to the water is 1: 1-5.
3. The method of claim 1, wherein in step (4), the zinc oxide has a particle size of less than 40 μm.
4. The method according to claim 3, wherein in step (4), the zinc oxide has a particle size of 500 nm.
5. The method of claim 1, wherein the temperature is maintained at 10-40 ℃ during step (5).
6. The method of claim 5, wherein the temperature is maintained at 25 ℃ during step (5).
7. The method of claim 1, wherein the pH is maintained at 8-10 during step (5).
8. The method of claim 7, wherein during step (5), the pH is maintained at 9.
9. The method according to claim 1, wherein in the step (7), the centrifugal screen has a pore size of 10 to 100 μm.
10. The method according to claim 9, wherein in step (7), the centrifugal screen has a pore size of 45 μm.
CN201811622624.1A 2017-12-28 2018-12-28 Post-treatment method of rare earth sulfide Active CN109651846B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201711457869 2017-12-28
CN2017114578699 2017-12-28

Publications (2)

Publication Number Publication Date
CN109651846A CN109651846A (en) 2019-04-19
CN109651846B true CN109651846B (en) 2021-01-05

Family

ID=66117888

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811622624.1A Active CN109651846B (en) 2017-12-28 2018-12-28 Post-treatment method of rare earth sulfide

Country Status (1)

Country Link
CN (1) CN109651846B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110591414A (en) * 2019-10-14 2019-12-20 包头中科世纪科技有限责任公司 Rare earth sulfide and/or rare earth oxysulfide colorant and preparation method thereof
CN112625464B (en) * 2020-12-01 2021-10-26 景德镇陶瓷大学 Preparation method of PEG (polyethylene glycol) and carbon powder refined cristobalite coated gamma-Ce 2S3 red pigment and product prepared by preparation method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1241987A (en) * 1996-11-19 2000-01-19 罗狄亚化学公司 Use of a beta rare earth sulphide as colouring pigment and method for preparing same
CN1426376A (en) * 2000-03-30 2003-06-25 罗狄亚稀土公司 Composition based on rare earth metal sulplide with improved chemical stability, its preparation method and use as pigment thereof
CN102770214A (en) * 2009-12-04 2012-11-07 巴里克黄金公司 Separation of cooper minerals from pyrite using air-metabisulfite treatment
CN103819934A (en) * 2014-02-25 2014-05-28 内蒙古大学 Method for preparing coated rare earth sulfide pigment
CN104289319A (en) * 2008-07-25 2015-01-21 塞特克技术公司 Flotation reagents and flotation processes utilizing same
CN106430274A (en) * 2016-08-29 2017-02-22 湖南科莱新材料有限公司 Method for preparing nano cerium sulfide by adopting liquid phase method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1241987A (en) * 1996-11-19 2000-01-19 罗狄亚化学公司 Use of a beta rare earth sulphide as colouring pigment and method for preparing same
CN1426376A (en) * 2000-03-30 2003-06-25 罗狄亚稀土公司 Composition based on rare earth metal sulplide with improved chemical stability, its preparation method and use as pigment thereof
CN104289319A (en) * 2008-07-25 2015-01-21 塞特克技术公司 Flotation reagents and flotation processes utilizing same
CN102770214A (en) * 2009-12-04 2012-11-07 巴里克黄金公司 Separation of cooper minerals from pyrite using air-metabisulfite treatment
CN103819934A (en) * 2014-02-25 2014-05-28 内蒙古大学 Method for preparing coated rare earth sulfide pigment
CN106430274A (en) * 2016-08-29 2017-02-22 湖南科莱新材料有限公司 Method for preparing nano cerium sulfide by adopting liquid phase method

Also Published As

Publication number Publication date
CN109651846A (en) 2019-04-19

Similar Documents

Publication Publication Date Title
CN111084727B (en) Method for preparing nano zinc oxide surface modification and reverse phase dispersion slurry
CN109651846B (en) Post-treatment method of rare earth sulfide
CN101475217B (en) Method for preparing pigment grade chromium hemitrioxide green by using gaseous reducing agent to reduce chromate salt under low temperature
CN103709833A (en) Polymer coated inorganic pigment paste for color modulation of production line and preparation method thereof
CN110075895A (en) A kind of carbon nitrence-zinc sulphide composite nano materials and its preparation method and application
CN102093779A (en) Environmental-protection water-based ink and preparation method thereof
CN104830099B (en) Coated silica-bismuth vanadate-barium sulfate high-brightness yellow pigment preparation method
CN103613958B (en) Environment-friendly titanium pigment prepared by using complexation-precipitation process
CN111748222B (en) High-tinting strength copper-chromium black pigment and preparation method thereof
CN112625464B (en) Preparation method of PEG (polyethylene glycol) and carbon powder refined cristobalite coated gamma-Ce 2S3 red pigment and product prepared by preparation method
CN103627217B (en) Environmentally-friendly titanium type pigment and process for preparing pigment by adopting grafting bridging method
CN113004757A (en) Dyed sand slurry, artificial colored sand and preparation method
CN110980786B (en) Method for simultaneously preparing nano calcium carbonate and chlorine-free calcium silicate early strength agent by using marble polishing waste residues
CN112048189A (en) System and method for preparing phthalocyanine blue P.B.15 by direct slurry acid swelling method
CN116751463B (en) Composite pigment coated with nano aluminum hydroxide and preparation method thereof
CN101659814B (en) Preparation method of water-borne polyurethane color paste
CN108250800B (en) High-temperature-resistant black nano pigment and application thereof
CN105505011B (en) Preparation method of aqueous environment-friendly nano color paste for synthetic leather coating
CN108587250B (en) Composite pigment surface modifier and application method thereof
CN110079111A (en) A kind of zinc ferrite/humic acid nanocomposite and its preparation method and application
CN102115618B (en) Extinction barium and preparation method thereof
CN108101118A (en) A kind of waste water extraction iron of iron content containing zinc and the method for preparing iron oxide
CN113502089A (en) Color paste for water-based pen ink
CN109790396B (en) Method for producing bismuth-based pigments with improved alkali resistance by encapsulating bismuth-based pigments with chelating agents
CN101220214A (en) Polymer type organic pigment and method for producing the same

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: A post-treatment method of rare earth sulfide

Effective date of registration: 20220411

Granted publication date: 20210105

Pledgee: Baotou Kundulun Mengyin Village Bank Co.,Ltd.

Pledgor: BAOTOU HONGBO TE TECHNOLOGY Co.,Ltd.

Registration number: Y2022150000030

PC01 Cancellation of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20230406

Granted publication date: 20210105

Pledgee: Baotou Kundulun Mengyin Village Bank Co.,Ltd.

Pledgor: BAOTOU HONGBO TE TECHNOLOGY Co.,Ltd.

Registration number: Y2022150000030

PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: A post-treatment method for rare earth sulfides

Effective date of registration: 20230407

Granted publication date: 20210105

Pledgee: Baotou Kundulun Mengyin Village Bank Co.,Ltd.

Pledgor: BAOTOU HONGBO TE TECHNOLOGY Co.,Ltd.

Registration number: Y2023150000058

PC01 Cancellation of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Granted publication date: 20210105

Pledgee: Baotou Kundulun Mengyin Village Bank Co.,Ltd.

Pledgor: BAOTOU HONGBO TE TECHNOLOGY Co.,Ltd.

Registration number: Y2023150000058

PE01 Entry into force of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of invention: A post-treatment method for rare earth sulfides

Granted publication date: 20210105

Pledgee: Baotou Kundulun Mengyin Village Bank Co.,Ltd.

Pledgor: BAOTOU HONGBO TE TECHNOLOGY Co.,Ltd.

Registration number: Y2024150000035