CN108504141A - A kind of method that liquid phase high temperature and pressure cladding prepares heatproof iron oxide yellow - Google Patents
A kind of method that liquid phase high temperature and pressure cladding prepares heatproof iron oxide yellow Download PDFInfo
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- CN108504141A CN108504141A CN201810195685.8A CN201810195685A CN108504141A CN 108504141 A CN108504141 A CN 108504141A CN 201810195685 A CN201810195685 A CN 201810195685A CN 108504141 A CN108504141 A CN 108504141A
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- iron oxide
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT 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
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/22—Compounds of iron
- C09C1/24—Oxides of iron
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT 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
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/006—Combinations of treatments provided for in groups C09C3/04 - C09C3/12
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT 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
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/06—Treatment with inorganic compounds
- C09C3/063—Coating
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT 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
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/08—Treatment with low-molecular-weight non-polymer organic compounds
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/32—Thermal properties
- C01P2006/37—Stability against thermal decomposition
Abstract
The present invention relates to ferric oxide yellow pigment more particularly to a kind of methods that liquid phase high temperature and pressure cladding prepares iron oxide yellow.This method includes the following steps:1) the iron oxide yellow slurries made are placed in reaction kettle, are slowly added to aluminum sulfate solution while stirring, then in the feed liquid during glycerine and zinc carbonate addition reaction kettle is added, it is 11 12 to adjust material liquid pH value in reaction kettle, after pH stabilizations, closes and reacts kettle cover;2) it starts to warm up to 220 DEG C 250 DEG C, after reactor temperature reaches 220 250 DEG C, into heat-insulation pressure keeping state;3) after keeping the temperature 13 hours, heating power supply is closed, but be kept stirring, until opening kettle cover after being cooled to 60 DEG C or less, it is 7.5~8.5 to be adjusted to pH, is rinsed, is filtered after pH stabilizations, 100 120 DEG C of dryings finally crush.The advantages that cladded type iron oxide yellow that the present invention synthesizes has heat resistance good, and cladding is more uniform, and synthetic method is simple, at low cost, safety and environmental protection.
Description
Technical field
The present invention relates to the sides that ferric oxide yellow pigment more particularly to a kind of liquid phase high temperature and pressure cladding prepare iron oxide yellow
Method.
Background technology
Iron oxide yellow, also known as FeOOH, molecular formula are FeOOH or Fe2O3·H2O is in yellow powder, grain
Sub- shape is needle-shaped, and it is environmentally friendly inorganic pigment, light resistance to have higher tinting strength, tinting power, covering power, and nontoxic
Reach 6-7 grades.Ferric oxide yellow pigment is widely used in building materials, coating, paint, plastics, rubber, electronics, industrial catalyst, cigarette
The industries such as grass, cosmetics.
Common iron oxide yellow surface is not coated, contained by the crystallization water be easy to lose at high temperature, to become
Iron oxide red.It is mainly at present the technology coated under room temperature about the coating technology of ferric oxide yellow pigment, due under room temperature,
Pigment particles often exist in a manner of reunion, also are difficult to by particle whole depolymerization, and just because of reunion grain by high-speed stirred
The presence of son causes coating to cannot be introduced into all cladding faces, uneven so as to cause coating, and influences heat resistance.
Chinese invention patent application (the application number of applicant's application:CN201710154320.6 a kind of heat resistant type) is disclosed
Ferric oxide yellow pigment and preparation method thereof, the composite material formed by trbasic zinc phosphate coated iron oxide Huang improve iron oxide yellow
Heat resistance can be used when plastic processing and powdery paints are applied as colorant and preservative.But prepared by this method
Iron oxide yellow is molded temperature tolerance can only be at 260 DEG C or so, and the cladding period of the common iron oxide yellow cladding process is longer, are 10-
Or so 20 hours.
Invention content
The present invention coats non-uniform deficiency to solve ferric oxide yellow pigment, influences heat resistance, the present invention first
Purpose is a kind of method that liquid phase high temperature and pressure cladding prepares iron oxide yellow, and this method is by being added glycerine, after capable of being dissolved in water
It is attached to scattered iron oxide yellow surface, it is made to be not easy to reunite so that the cladding of aluminium is more uniform, in addition, passing through high temperature height
It is only the 1/10-1/ in common iron oxide yellow cladding period that pressure reaction condition, which can promote the promotion of coating efficiency, cladding period,
5, further, the present invention improves iron oxide yellow heat resistance in one layer of compact aluminum oxide of iron oxide yellow outer cladding and zinc oxide film
Energy.
In order to achieve the above purpose, present invention employs technical solutions below:
A kind of method that liquid phase high temperature and pressure cladding prepares iron oxide yellow, this method include the following steps:
1) the iron oxide yellow slurries made are placed in reaction kettle, open stirring, is slowly added to aluminum sulfate solution while stirring, so
Afterwards in the feed liquid during glycerine and zinc carbonate addition reaction kettle is added, it is 11~12 to adjust material liquid pH value in reaction kettle, waits for pH
After stabilization, reaction kettle cover is closed;The addition of the aluminum sulfate is the 40~60% of iron oxide yellow weight, and the addition of glycerine is
The 1%~5% of iron oxide yellow weight, the addition of zinc carbonate are the 2~8% of iron oxide yellow weight;
2) it starts to warm up to 250 DEG C -300 DEG C, heating rate controls within per minute at 5~15 DEG C;When warm in reaction kettle
After degree reaches 220-250 DEG C, into keeping warm mode, pressure control is in 2.2-4.0MPA, and heat preservation temperature difference control is within 5 DEG C;
3) after keeping the temperature 1-3 hours, heating power supply is closed, but be kept stirring, until kettle cover is opened after being cooled to 60 DEG C or less,
It is 7.5~8.5 to be adjusted to pH, is rinsed, is filtered after pH stabilizations, 100-120 DEG C of drying finally crushes.
As a further improvement, the addition of the aluminum sulfate is the 45-55% of iron oxide yellow weight, the addition of glycerine
It is the 1.6%~3.5% of iron oxide yellow weight, the addition of zinc carbonate is the 2.7~5.0% of iron oxide yellow weight.
As a further improvement, the mass percent concentration of the iron oxide yellow slurries is 8~15%;It will be prepared after preparing
Good iron oxide yellow slurries, which are placed in high speed dispersion stirring, carries out dispersion stirring, and rotating speed is controlled in 500R/min, and jitter time is
30-40 minutes.
As a further improvement, the mass percent concentration of the aluminum sulfate be 15~25%, use content for
The Al of 98.5% mass fraction2(SO4)3·16H2O, which is prepared, to be made.
As a further improvement, adjusting pH value, step using the NaoH solution of 10% mass fraction in the step 1)
3) pH value is adjusted using the dilute sulfuric acid of 10% mass fraction in.
The present invention is attached to scattered iron oxide yellow surface after capable of being dissolved in water, makes its group of being not easy by the way that glycerine is added
It is poly- so that the cladding of aluminium is more uniform, and further, the present invention uses high temperature and pressure powder deploymerization and decentralization technology, passes through aluminium oxide
The composite material formed with oxide coated by zinc iron oxide yellow improves the heat resistance of iron oxide yellow, can be applied in plastic processing and powder
It is used as colorant and preservative when material application, simultaneous oxidation zinc can to a certain degree inhibit the red phase of later stage iron oxide yellow
Generation so that color is purer.In addition, it is desirable to reach 260 DEG C or more of temperature tolerance, after common iron oxide yellow coats, cladding
The percentage that object accounts for iron oxide yellow total amount reaches 20% or more, directly affects power part and the form and aspect of iron oxide yellow, and after this technique cladding,
Coating accounting only 10% or so, power part higher, power part that difference is about 10% or so.The cladded type iron oxide that the present invention synthesizes
Huang has heat resistance good, and cladding is more uniform, and synthetic method is simple, the cladding period is short, the only commonly 1/10- in cladding period
1/5, the advantages that at low cost, safety and environmental protection, there is higher industrial application value.
Specific implementation mode
Embodiment 1:
1. 750g iron oxide yellow dry powder is taken to be added in 14250g water, being configured to the iron oxide yellow slurries of 15000g, (volume is about
For 15L).2. prepared iron oxide yellow slurries are placed in high speed dispersion stirring and carry out dispersion stirring, rotating speed is controlled in 500R/
Min, jitter time are 30-40 minutes.
3. by the Al that content is 98.5% mass fraction2(SO4)3·16H2O solids 404g is added in 1500g water fully
Dissolving is configured to the aluminum sulfate solution that mass fraction is 21.2%.
4. weighing SILVER REAGENT glycerine and zinc carbonate, the amount of glycerine is 20ml, and the amount of zinc carbonate is 30g.
5. the prepared 15000g iron oxide yellows slurries of the 1st step are placed in reaction kettle, stirring is opened, mixing speed control exists
150R/min is slowly added to prepared 1904g aluminum sulfate solutions in the 3rd step, and time control is added in 180S or so, then exists
It is added in the feed liquid that third walks in prepared glycerine and zinc carbonate addition reaction kettle, after 2min, utilizes 10% mass fraction
NaoH solution adjust reaction kettle in material liquid pH value be 11.5, after pH stabilization after, close reaction kettle cover.
6. starting to warm up to 220 DEG C, heating rate controls within per minute at 10 DEG C.When reactor temperature reaches 220
After DEG C, into keeping warm mode, in 2.25MPA, soaking time is 1 hour for pressure control, and heat preservation temperature difference control is within 5 DEG C.
7. after heat preservation 1 hour, closing heating power supply, but be kept stirring, until opening kettle cover after being cooled to 60 DEG C or less, use
It is 8 that 10% dilute sulfuric acid, which is adjusted to pH, is rinsed, is filtered after pH stabilizations, 100-120 DEG C of drying finally crushes.Obtain sample
Product A.
Embodiment 2:
1. 750g iron oxide yellow dry powder is taken to be added in 14250g water, being configured to the iron oxide yellow slurries of 15000g, (volume is about
For 15L).2. prepared iron oxide yellow slurries are placed in high speed dispersion stirring and carry out dispersion stirring, rotating speed is controlled in 500R/
Min, jitter time are 30-40 minutes.
3. by the Al that content is 98.5% mass fraction2(SO4)3·16H2O solids 350g is added in 1500g water fully
Dissolving is configured to the aluminum sulfate solution that mass fraction is 21.2%.
4. weighing SILVER REAGENT glycerine and zinc carbonate, the amount of glycerine is 15ml, and the amount of zinc carbonate is 25g.
5. the prepared 15000g iron oxide yellows slurries of the 1st step are placed in reaction kettle, stirring is opened, mixing speed control exists
150R/min is slowly added to prepared 1850g aluminum sulfate solutions in the 3rd step, and time control is added in 180S or so, then exists
It is added in the feed liquid that third walks in prepared glycerine and zinc carbonate addition reaction kettle, after 2min, utilizes 10% mass fraction
NaoH solution adjust reaction kettle in material liquid pH value be 11.5, after pH stabilization after, close reaction kettle cover.
6. starting to warm up to 227 DEG C, heating rate controls within per minute at 10 DEG C.When reactor temperature reaches 227
After DEG C, into keeping warm mode, in 2.5MPA, soaking time is 1 hour for pressure control, and heat preservation temperature difference control is within 5 DEG C.
7. after heat preservation 1 hour, closing heating power supply, but be kept stirring, until opening kettle cover after being cooled to 60 DEG C or less, use
It is 8 that 10% dilute sulfuric acid, which is adjusted to pH, is rinsed, is filtered after pH stabilizations, 100-120 DEG C of drying finally crushes.Obtain sample
Product B.
Embodiment 3
1. 750g iron oxide yellow dry powder is taken to be added in 14250g water, being configured to the iron oxide yellow slurries of 15000g, (volume is about
For 15L).2. prepared iron oxide yellow slurries are placed in high speed dispersion stirring and carry out dispersion stirring, rotating speed is controlled in 500R/
Min, jitter time are 30-40 minutes.
3. by the Al that content is 98.5% mass fraction2(SO4)3·16H2O solids 440g is added in 1500g water fully
Dissolving is configured to the aluminum sulfate solution that mass fraction is 21.2%.
4. weighing SILVER REAGENT glycerine and zinc carbonate, the amount of glycerine is 26ml, and the amount of zinc carbonate is 37g.
5. the prepared 15000g iron oxide yellows slurries of the 1st step are placed in reaction kettle, stirring is opened, mixing speed control exists
150R/min is slowly added to prepared 1940g aluminum sulfate solutions in the 3rd step, and time control is added in 180S or so, then exists
It is added in the feed liquid that third walks in prepared glycerine and zinc carbonate addition reaction kettle, after 2min, utilizes 10% mass fraction
NaoH solution adjust reaction kettle in material liquid pH value be 11.5, after pH stabilization after, close reaction kettle cover.
6. starting to warm up to 225 DEG C, heating rate controls within per minute at 10 DEG C.When reactor temperature reaches 225
After DEG C, into keeping warm mode, in 2.45MPA, soaking time is 1 hour for pressure control, and heat preservation temperature difference control is within 5 DEG C.
7. after heat preservation 3 hours, closing heating power supply, but be kept stirring, until opening kettle cover after being cooled to 60 DEG C or less, use
It is 8 that 10% dilute sulfuric acid, which is adjusted to pH, is rinsed, is filtered after pH stabilizations, 100-120 DEG C of drying finally crushes.Obtain sample
Product C.
Embodiment 4
1. 1500g iron oxide yellow dry powder is taken to be added in 14250g water, being configured to the iron oxide yellow slurries of 15000g, (volume is about
For 15L).2. prepared iron oxide yellow slurries are placed in high speed dispersion stirring and carry out dispersion stirring, rotating speed is controlled in 500R/
Min, jitter time are 30-40 minutes.
3. by the Al that content is 98.5% mass fraction2(SO4)3·16H2O solids 450g is added in 1500g water fully
Dissolving is configured to the aluminum sulfate solution that mass fraction is 21.2%.
4. weighing SILVER REAGENT glycerine and zinc carbonate, the amount of glycerine is 25ml, and the amount of zinc carbonate is 20g.
5. the prepared 15000g iron oxide yellows slurries of the 1st step are placed in reaction kettle, stirring is opened, mixing speed control exists
150R/min is slowly added to prepared 1950g aluminum sulfate solutions in the 3rd step, and time control is added in 180S or so, then exists
It is added in the feed liquid that third walks in prepared glycerine and zinc carbonate addition reaction kettle, after 2min, utilizes 10% mass fraction
NaoH solution adjust reaction kettle in material liquid pH value be 11.5, after pH stabilization after, close reaction kettle cover.
6. starting to warm up to 222 DEG C, heating rate controls within per minute at 10 DEG C.When reactor temperature reaches 222
After DEG C, into keeping warm mode, in 2.35MPA, soaking time is 1 hour for pressure control, and heat preservation temperature difference control is within 5 DEG C.
7. after heat preservation 3 hours, closing heating power supply, but be kept stirring, until opening kettle cover after being cooled to 60 DEG C or less, use
It is 8 that 10% dilute sulfuric acid, which is adjusted to pH, is rinsed, is filtered after pH stabilizations, 100-120 DEG C of drying finally crushes.Obtain sample
Product D.
Comparative example (does not add glycerine and zinc carbonate)
1. 750g iron oxide yellow dry powder is taken to be added in 14250g water, being configured to the iron oxide yellow slurries of 15000g, (volume is about
For 15L).2. prepared iron oxide yellow slurries are placed in high speed dispersion stirring and carry out dispersion stirring, rotating speed is controlled in 500R/
Min, jitter time are 30-40 minutes.
3. by the Al that content is 98.5% mass fraction2(SO4)3·16H2O solids 450g is added in 1500g water fully
Dissolving is configured to the aluminum sulfate solution that mass fraction is 21.2%.
5. the prepared 15000g iron oxide yellows slurries of the 1st step are placed in reaction kettle, stirring is opened, mixing speed control exists
150R/min is slowly added to prepared 1950g aluminum sulfate solutions in the 3rd step, and time control is added in 180S or so, then exists
It is added in the feed liquid that third walks in prepared glycerine and zinc carbonate addition reaction kettle, after 2min, utilizes 10% mass fraction
NaoH solution adjust reaction kettle in material liquid pH value be 11.5, after pH stabilization after, close reaction kettle cover.
6. starting to warm up to 223 DEG C, heating rate controls within per minute at 10 DEG C.When reactor temperature reaches 223
After DEG C, into keeping warm mode, in 2.35MPA, soaking time is 1 hour for pressure control, and heat preservation temperature difference control is within 5 DEG C.
7. after heat preservation 3 hours, closing heating power supply, but be kept stirring, until opening kettle cover after being cooled to 60 DEG C or less, use
It is 8 that 10% dilute sulfuric acid, which is adjusted to pH, is rinsed, is filtered after pH stabilizations, 100-120 DEG C of drying finally crushes.Obtain sample
Product E.
Detection:To five samples of ABCDE by the 4.1st article in HG/T 3853-2006 standards to the iron oxide after cladding
Huang carries out 280 DEG C of high-temperature process, is carrying out pigment color comparison by GB/T1864-2012, color is carried out using colour photometer
It measures, obtains 280 DEG C of the samples of ABCDE five/dry powder heat resistance test in 30 minutes:
Sample | △E |
Common iron oxide yellow | > 20.00 |
A | 2.53 |
B | 2.16 |
C | 2.48 |
D | 1.98 |
E | 5.25 |
Claims (5)
1. a kind of method that liquid phase high temperature and pressure cladding prepares heatproof iron oxide yellow, which is characterized in that this method includes below
Step:
1) the iron oxide yellow slurries made are placed in reaction kettle, open stirring, is slowly added to aluminum sulfate solution while stirring, then exists
Glycerine is added and zinc carbonate is added in the feed liquid in reaction kettle, it is 11~12 to adjust material liquid pH value in reaction kettle, waits for that pH stablizes
Afterwards, reaction kettle cover is closed;The addition of the aluminum sulfate is the 40~60% of iron oxide yellow weight, and the addition of glycerine is iron oxide yellow
The 1%~5% of weight, the addition of zinc carbonate are the 2~8% of iron oxide yellow weight;
2) it starts to warm up to 250 DEG C -300 DEG C, heating rate controls within per minute at 5~15 DEG C;When reactor temperature reaches
To after 220-250 DEG C, into keeping warm mode, pressure control is in 2.2-4.0MPA, and heat preservation temperature difference control is within 5 DEG C;
3) after keeping the temperature 1-3 hours, heating power supply is closed, but be kept stirring, until opening kettle cover after being cooled to 60 DEG C or less, adjusted
It is 7.5~8.5 to pH, is rinsed, filtered after pH stabilizations, 100-120 DEG C of drying finally crushes.
2. the method that a kind of liquid phase high temperature and pressure cladding according to claim 1 prepares iron oxide yellow, which is characterized in that institute
The addition for the aluminum sulfate stated is the 45-55% of iron oxide yellow weight, and the addition of glycerine is the 1.6%~3.5% of iron oxide yellow weight,
The addition of zinc carbonate is the 2.7~5.0% of iron oxide yellow weight.
3. the method that a kind of liquid phase high temperature and pressure cladding according to claim 1 prepares iron oxide yellow, which is characterized in that profit
With water is added in iron oxide yellow dry powder, the mass percent concentration of control iron oxide yellow slurries is 8~15%;It will be prepared after preparing
Iron oxide yellow slurries be placed in high speed dispersion stirring and carry out dispersion stirring, rotating speed is controlled in 500R/min, jitter time 30-
40 minutes.
4. the method that a kind of liquid phase high temperature and pressure cladding according to claim 1 prepares iron oxide yellow, which is characterized in that sulphur
The mass percent concentration of sour aluminium is 15~25%, uses content for the Al of 98.5% mass fraction2(SO4)3·16H2O is prepared
It is made.
5. the method that a kind of liquid phase high temperature and pressure cladding according to claim 1 prepares iron oxide yellow, which is characterized in that step
Rapid 1) the middle NaoH solution using 10% mass fraction adjusts pH value, and the dilute sulfuric acid adjusting of 10% mass fraction is used in step 3)
PH value.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1566216A (en) * | 2003-06-10 | 2005-01-19 | 上海凯丽氧化铁有限公司 | Process and formula for preparing fire-resistant zinc-iron yellow pigment |
CN102001712A (en) * | 2010-12-16 | 2011-04-06 | 苏州康立达纳米生物工程有限公司 | Method for preparing superparamagnetic Fe3O4 nano particle based on thermal decomposition of template |
CN104667945A (en) * | 2015-01-10 | 2015-06-03 | 安徽大学 | Preparation of supported palladium catalyst Fe3O4/SiO2/Pd and application of supported palladium catalyst Fe3O4/SiO2/Pd in Suzuki reaction |
CN105802699A (en) * | 2016-04-14 | 2016-07-27 | 合肥师范学院 | Ferroferric oxide/ tungsten disulfide nano-composite lubricating agent and preparation method thereof |
-
2018
- 2018-03-09 CN CN201810195685.8A patent/CN108504141A/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1566216A (en) * | 2003-06-10 | 2005-01-19 | 上海凯丽氧化铁有限公司 | Process and formula for preparing fire-resistant zinc-iron yellow pigment |
CN102001712A (en) * | 2010-12-16 | 2011-04-06 | 苏州康立达纳米生物工程有限公司 | Method for preparing superparamagnetic Fe3O4 nano particle based on thermal decomposition of template |
CN104667945A (en) * | 2015-01-10 | 2015-06-03 | 安徽大学 | Preparation of supported palladium catalyst Fe3O4/SiO2/Pd and application of supported palladium catalyst Fe3O4/SiO2/Pd in Suzuki reaction |
CN105802699A (en) * | 2016-04-14 | 2016-07-27 | 合肥师范学院 | Ferroferric oxide/ tungsten disulfide nano-composite lubricating agent and preparation method thereof |
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Title |
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Application publication date: 20180907 |